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JPH0617317B2 - Free-flowing powder composition - Google Patents
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JPH0617317B2 - Free-flowing powder composition - Google Patents

Free-flowing powder composition

Info

Publication number
JPH0617317B2
JPH0617317B2 JP60078051A JP7805185A JPH0617317B2 JP H0617317 B2 JPH0617317 B2 JP H0617317B2 JP 60078051 A JP60078051 A JP 60078051A JP 7805185 A JP7805185 A JP 7805185A JP H0617317 B2 JPH0617317 B2 JP H0617317B2
Authority
JP
Japan
Prior art keywords
powder
mfc
adsorbed
free
present
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.)
Expired - Lifetime
Application number
JP60078051A
Other languages
Japanese (ja)
Other versions
JPS61236731A (en
Inventor
示 本山
誠一 梅田
龍二 池間
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.)
Freund Corp
Original Assignee
Freund Corp
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 Freund Corp filed Critical Freund Corp
Priority to JP60078051A priority Critical patent/JPH0617317B2/en
Publication of JPS61236731A publication Critical patent/JPS61236731A/en
Publication of JPH0617317B2 publication Critical patent/JPH0617317B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/02Cosmetics or similar toiletry preparations characterised by special physical form
    • A61K8/0241Containing particulates characterized by their shape and/or structure
    • A61K8/027Fibers; Fibrils
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/72Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds
    • A61K8/73Polysaccharides
    • A61K8/731Cellulose; Quaternized cellulose derivatives
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61QSPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
    • A61Q1/00Make-up preparations; Body powders; Preparations for removing make-up
    • A61Q1/12Face or body powders for grooming, adorning or absorbing

Landscapes

  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Epidemiology (AREA)
  • Birds (AREA)
  • Cosmetics (AREA)
  • General Preparation And Processing Of Foods (AREA)
  • Jellies, Jams, And Syrups (AREA)
  • Seasonings (AREA)
  • Formation And Processing Of Food Products (AREA)
  • Non-Alcoholic Beverages (AREA)
  • Medicinal Preparation (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は吸湿性の高い医薬性、化粧品又は食品を高相対
湿度下にても流動性の優れ取扱い容易な粉粒体である組
成物に関する。
TECHNICAL FIELD The present invention relates to a composition which is a granular material which has excellent hygroscopicity and has excellent fluidity and is easy to handle even under high relative humidity in pharmaceuticals, cosmetics or foods. .

(従来技術) 従来、吸湿性の高い医薬性や食品例えば、粉末ジユー
ス、粉ミルク、アミノ酸系調味料、食肉類エキス、生薬
抽出物、エタンブトール、塩化コリン、テオフイリン、
ビタミンU、メチオニン等は吸湿性が強く、その粉末を
大気中にて放置すると、吸湿してブロツキングしたり、
潮解したりして取扱いが困難であつた。これを改善する
目的で、これらの物質を軽質無水珪酸や結晶セルロース
等に吸着、担持させてブロツキング性を去し易流動性の
粉末とすることが行なわれてきた。しかし、軽質無水珪
酸を使用すると、食品には利用不可能であり、医薬品と
しては、打錠成形性が不良で、他の賦形剤を添加しなけ
ればならず、又軽質無水珪酸は固体酸で、医薬品の分解
を招くなどの欠点がある。結晶セルローズを使用する
と、吸着能があまり大きくないため、吸湿物質に対し
て、多量に加える必要がある。又食品に適用したとしき
には、ザラついて口あたりが不良である。又製造過程で
塩酸などを使用した結晶セルロースにあつては、渋味、
えぐい味等の異味を示すなどの欠点があつた。
(Prior art) Conventionally, highly hygroscopic pharmaceuticals and foods, for example, powdered youth, powdered milk, amino acid-based seasonings, meat extracts, herbal medicine extracts, ethambutol, choline chloride, theophylline,
Vitamin U, methionine, etc. have strong hygroscopicity, and if the powder is left in the air, it will absorb moisture and block,
It was difficult to handle due to deliquescence. For the purpose of improving this, it has been performed that these substances are adsorbed on and supported by light anhydrous silicic acid, crystalline cellulose and the like to remove the blocking property and become a free-flowing powder. However, when light anhydrous silicic acid is used, it cannot be used in foods, it has poor tableting moldability as a drug, and other excipients must be added. However, there are drawbacks such as the decomposition of pharmaceutical products. When crystalline cellulose is used, its adsorption ability is not so large, so it is necessary to add a large amount to the hygroscopic substance. Moreover, when it is applied to food, it has a rough texture and a bad mouth feel. For crystalline cellulose that uses hydrochloric acid, etc. in the manufacturing process,
There were drawbacks such as showing a bad taste such as astringent taste.

(発明の目的) 本発明は、これらの欠点を改良した吸湿性物質を含む易
流動性粉粒体組成物を提供するものである。この組成物
は吸湿性の高い物質と微小繊維状セルロース(以下MF
Cという)とからなるものである。
(Object of the Invention) The present invention provides a free-flowing powdery or granular material composition containing a hygroscopic substance in which these drawbacks are improved. This composition consists of highly hygroscopic substances and microfibrous cellulose (hereinafter MF
It is called C).

(発明の構成) 本発明者らは、記の吸湿性の高い物質を効率良く、取扱
い易い易流動性の粉粒体とする方法について鋭意研究を
重ねた結果、MFCは従来広く使用されている結晶セル
ロースと類似の物質であるにも拘らず、MFCはこれに
吸湿性物質を吸着させた粉粒体が、従来一般に広く使用
されていた結晶セルロースに吸湿性物質を吸着させた粉
粒体に比して格段に耐湿安定性が良く、且食品とした場
合意外にも異味がなく口当りが良いこと見出し、本発明
に到達した。
(Structure of the Invention) As a result of intensive studies conducted by the present inventors on a method of efficiently converting the substance having high hygroscopicity into a free-flowing powdery granule, MFC has been widely used in the past. Despite being a substance similar to crystalline cellulose, MFC has a granular material in which a hygroscopic substance is adsorbed to this, but is a granular substance in which a hygroscopic substance is adsorbed to crystalline cellulose that has been widely used in the past. In comparison, the present inventors have found that the moisture resistance stability is remarkably good, and that when it is used as a food, it does not have an unpleasant taste and has a pleasant mouthfeel, and the present invention has been completed.

本発明の要旨は「吸湿性の高い医薬品、化粧品又は食品
に微小繊維状セルロースを添加分散してなる易流動性粉
粒体組成物」である。
The gist of the present invention is "a free-flowing powdery or granular material composition obtained by adding and dispersing fine fibrous cellulose to a drug, cosmetics or food having high hygroscopicity".

なお、本発明に係る微小繊維セルロース(ダイセル化学
工業がMFCの名称で製造販売している)は、パルプを
水に懸濁させ、高剪断力下で叩解して、セルロース繊維
を物理的に直径約1μ以下のミクロフイブリル化して得
られるもので、前述の従来一般に広く使用されている結
晶セルロースとは明確に異るものである。結晶セルロー
スは「アビセル」(登録商標)の名で市販されている。
結晶セルロースは高純度の天然セルロースを鉱酸加水分
解し、非結晶部分を除去し結晶部分を取出して精製し乾
燥したものである。この本発明の組成物に係る微小繊維
状セルロースは、従来は2重量%程度の水中懸濁液とし
て市販され、食品工業などに於て増粘剤として利用され
ている。
In addition, the microfiber cellulose (manufactured and sold by Daicel Chemical Industries under the name of MFC) according to the present invention is prepared by suspending pulp in water and beating it under a high shearing force to physically divide the cellulose fiber into a diameter. It is obtained by forming microfibrils of about 1 μm or less, which is distinctly different from the above-mentioned crystalline cellulose which has been widely used conventionally. Microcrystalline cellulose is commercially available under the name "Avicel" (registered trademark).
Crystalline cellulose is obtained by hydrolyzing high-purity natural cellulose with a mineral acid, removing the non-crystalline portion, extracting the crystalline portion, purifying and drying. The microfibrous cellulose according to the composition of the present invention is conventionally marketed as a suspension in water of about 2% by weight and used as a thickener in the food industry and the like.

本発明者らは、このMFCを水中懸濁液のまゝ、又はこ
れを脱水粉末化したものを使用して、吸湿性物質を処理
し本発明の易流動性粉粒体組成物を得ることに成功した
のである。
The present inventors obtain a free-flowing powdery or granular material composition of the present invention by treating a hygroscopic substance using the MFC as a suspension in water or dehydrated powder thereof. Was successful.

本発明に使用される吸湿性の高い食品又は医薬品として
は、粉末ジユース、粉ミルク、調味料類、食肉エキス
末、魚介類のエキス末、酵母類の抽出エキス末等の食
品、エタンブトール、塩化コリン、ビタミンU、メチオ
ニン、塩化リチウム、生薬抽出物末等の医薬品が例示さ
れ、吸湿性の高いという属性は具体的には、乾燥状態に
おけるその物質の粉末が常温、50%の相対湿度下にお
いて7日以内にブロツキングすることを意味する。な
お、注意を要することは本発明の原料として使用される
医薬品又は食品は粉末状のものに限られるのでなく溶液
状又は分散液状のものも含むことである。例えば粉末ジ
ユースの代りにジユース液そのものに微小繊維状セルロ
ースを添加分散し、この液を噴霧乾燥して、本発明の易
流動性粉粒体組成物を得ることが出来る。
The highly hygroscopic food or drug used in the present invention, powdered diuse, powdered milk, seasonings, meat extract powder, seafood extract powder, food products such as yeast extract powder, ethambutol, choline chloride, Drugs such as vitamin U, methionine, lithium chloride, powdered crude drug, etc. are exemplified, and the attribute of high hygroscopicity is specifically that the powder of the substance in a dry state is at room temperature and 50% relative humidity for 7 days. Means to block within. It should be noted that the drug or food used as the raw material of the present invention is not limited to the powder form, but may include the solution form or the dispersion form. For example, the free-flowing powdery or granular material composition of the present invention can be obtained by adding and dispersing the microfibrous cellulose to the diuse liquid itself instead of the powder diuse, and spray-drying this liquid.

上記の説明と一部重複するが、本発明組成物を得るに
は、吸湿性物質の粉末にMFCの粉末を適宜の割合で混
合してもよく、またMFC水中懸濁液に吸湿性物質を溶
解するか、エキス等にあつては、原料のエキスを液状で
MFCの水中懸濁液に添加した混合液を噴霧乾燥、凍結
乾燥など適当な手段で乾燥粉末化してもよい。
Although partially overlapping with the above description, in order to obtain the composition of the present invention, the powder of the hygroscopic substance may be mixed with the powder of MFC at an appropriate ratio, and the hygroscopic substance may be added to the suspension in MFC in water. In the case of being dissolved or in the case of an extract or the like, a mixed solution obtained by adding a raw material extract in a liquid state to a suspension of MFC in water may be dried and powdered by an appropriate means such as spray drying or freeze drying.

本発明組成物は、従来一般に広く使用されていた結晶セ
ルロースを用いて粉末化したものに比して、高湿度の環
境下でもブロツキングがなく、流動性を保持するもので
ある。本発明組成物は主として食品、医薬品及び化粧品
の原料として利用価値が大きい。又本発明組成物は、他
の物質と配合し易いので配合原料として食品、医薬品等
に利用される。
The composition of the present invention does not cause blocking even in an environment of high humidity and retains fluidity, as compared with a powdered product of crystalline cellulose that has been widely used in the past. The composition of the present invention has great utility mainly as a raw material for foods, pharmaceuticals and cosmetics. Further, since the composition of the present invention is easily mixed with other substances, it is used as a raw material for foods, pharmaceuticals and the like.

次に本発明組成物の製造法、実施例及びその本発明の実
施例の流動性に関し比較例と対比した試験を示めし、本
発明組成物を具体的に説明し、且その効果を明確にす
る。但し本発明はこれらの実施例等の記載により何ら限
定されるものではない。
Next, a method for producing the composition of the present invention, an example and tests for comparing the fluidity of the example of the present invention with those of the comparative example are shown to specifically explain the composition of the present invention and to clarify the effect thereof. To do. However, the present invention is not limited to the description of these examples.

実施例及びその試験 (1)50%濃度酵母抽出エキス末吸着MFC粉末 吸湿性の非常に高い酵母抽出エキス末100gを水:エ
タノール(4:1)混液150gに溶解し、それをビー
カー内で100gのMFC粉末と撹拌混合し、乾燥後混
合粉末を得た。この粉末が50%濃度酵母抽出エキス末
吸着MFC粉末である。同様な方法でMFC粉末の代り
に結晶セルロース及び軽質無水珪酸を使用し、それぞれ
50%濃度酵母抽出エキス末吸着結晶セルロース粉末及
び50%濃度酵母抽出エキス末吸着軽質無水珪酸粉末を
得た。
Examples and Tests (1) 50% Yeast Extract Extract Powder Adsorbing MFC Powder 100 g of yeast extract powder having a very high hygroscopic property was dissolved in 150 g of a water: ethanol (4: 1) mixed solution, and 100 g of the solution was mixed in a beaker. Stir-mixed with the MFC powder of 1. and dried to obtain a mixed powder. This powder is 50% concentrated yeast extract powder adsorbed MFC powder. In the same manner, crystalline cellulose and light anhydrous silicic acid were used instead of MFC powder to obtain 50% concentrated yeast extract extract powder-adsorbed crystalline cellulose powder and 50% concentrated yeast extract powder adsorbed light anhydrous silicic acid powder, respectively.

(2)(1)で得られた3種類の粉末を25℃75%RH(RHは
相対湿度以下同様)の条件下で24時間放置し、それら
の流動性につき、次の比較試験及びを行い、その結
果を表Iに示した。
(2) The three kinds of powders obtained in (1) were allowed to stand for 24 hours under the conditions of 25 ° C and 75% RH (RH is the same as the relative humidity below), and the following comparative tests and The results are shown in Table I.

安息角測定:野工、杉原式に準ずる。Angle of repose measurement: According to the fieldwork and Sugihara formula.

粘着度試験 下段から順に200,100,60メツシユのスクリー
ンを重ね、サンプルの粉体2gを最上段の60メツシユ
スクリーンの上に静かに置く、次に3個のスクリーンを
同時に120秒間振動させて振動停止後、目の粗いスク
リーンの上に残つた粉体の重量を測定し、2gに対する
%で粘着度を表す。但し、60メツシユは全部通過して
100メツシユの上に残つていれば、この量を測り2g
に対する%を求めこれの3/5の値を粘着度とする。10
0メツシユを全部通過し、200メツシユの上に残つた
場合は、1/5を乗じて粘着度とする。もし、2g全部が
200メツシユを通過すれば、粘着度0である。
Adhesion test 200, 100, 60 mesh screens were stacked in order from the bottom, and 2 g of the sample powder was gently placed on the top 60 mesh screen, then the three screens were simultaneously vibrated for 120 seconds. After stopping the vibration, the weight of the powder left on the coarse screen is measured and the degree of adhesion is expressed in% to 2 g. However, if all 60 mesh passes and remains above 100 mesh, measure this amount to 2 g.
% Is calculated and the value of 3/5 of this is taken as the tackiness. 10
If all 0 meshes are passed and 200 meshes are left, multiply by 1/5 to obtain the tackiness. If all 2 g pass through 200 mesh, the tack is 0.

(3)70%濃度酵母抽出エキス末吸着MFC粉末 酵母抽出エキス末140gとMFC粉末60gを使用し
(1)と同様の操作方法で、70%濃度酵母抽出エキス末
吸着MFC粉末を得た。同様にして70%濃度酵母抽出
エキス末吸着結晶セルロース粉末及び70%濃度酵母抽
出エキス末吸着軽質無水珪酸粉末を得た。
(3) 70% Yeast Extract Extract Powder Adsorbed MFC Powder Using 140 g of yeast extract powder and 60 g of MFC powder
By the same operation method as in (1), 70% concentration yeast extract extract powder-adsorbed MFC powder was obtained. Similarly, a 70% concentration yeast extract powder adsorbed crystalline cellulose powder and a 70% yeast extract powder adsorbed light anhydrous silicic acid powder were obtained.

(4)(3)で得られた粉末を用い、(2)と同じ条件で流動性
に関して安息角及び粘着度の試験を行い、その結果を表
Iに示した。
(4) Using the powder obtained in (3), the angle of repose and the tackiness were tested for fluidity under the same conditions as in (2), and the results are shown in Table 1.

(5)70%濃度酵母抽出エキス末の流動層による吸着M
FC粉末 吸湿性の非常に高い酵母抽出エキス末700gを水:エ
タノール(4:1)1,250g混液に溶解し、これを
スプレー液とする。この液をフローコーター・ミニ(フ
ロイント産業社製)の流動層を用いて、MFC粉末30
0gにスプレーし吸着させた。これで得た粉末を70%
濃度酵母抽出エキス末の流動層による吸着MFC粉末と
する。同様にして結晶セルロース及び軽質無水珪酸を用
い、70%濃度酵母抽出エキス末の流動層による吸着結
晶セルロース粉末及び70%濃度酵母抽出エキス末の流
動層による吸着軽質無水珪酸粉末を得た。
(5) Adsorption M of 70% concentrated yeast extract powder by fluidized bed
FC powder 700 g of yeast extract powder having a very high hygroscopic property is dissolved in a mixed solution of water and ethanol (4: 1, 1,250 g) to prepare a spray liquid. This liquid was mixed with MFC powder 30 using a fluidized bed of Flow Coater Mini (manufactured by Freund Corporation).
It was sprayed and adsorbed on 0 g. 70% of the powder thus obtained
Adsorbed MFC powder in a fluidized bed of concentrated yeast extract powder. Similarly, crystalline cellulose and light anhydrous silicic acid were used to obtain crystalline cellulose powder adsorbed by a fluidized bed of 70% concentrated yeast extract powder and adsorbed light anhydrous silicic acid powder by a fluidized bed of 70% yeast extract powder.

(6)(5)で得た各粉末に対して(2)と同じ条件で流動性に
関して安息角及び粘着度の比較試験を行つた。その結果
を表Iに示した。
(6) With respect to each of the powders obtained in (5), a comparative test was conducted on the fluidity under the same conditions as in (2) regarding the angle of repose and the degree of adhesion. The results are shown in Table I.

(7)50%濃度葛根湯末吸着MFC粉末 吸湿性の非常に高い葛根湯末100gを水150gに溶
かし、それにMFC粉末を100gを撹拌混合した後噴
霧乾燥し粉末を得た。これを50%濃度葛根湯末吸着M
FC粉末とする。同様な方法で軽質無水珪酸についても
行い、50%濃度葛根湯末吸着軽質無水珪酸粉末を得
た。
(7) 50% concentration Kakkonto powder adsorbed MFC powder 100 g of Kakkonto powder having a very high hygroscopicity was dissolved in 150 g of water, and 100 g of MFC powder was stirred and mixed, followed by spray drying to obtain a powder. This is 50% concentration Kakkonto powder adsorption M
FC powder. The same procedure was performed for light anhydrous silicic acid to obtain a 50% concentrated Kakkonto powder adsorbed light anhydrous silicic acid powder.

(8)(7)で得た粉末を用い(2)と同じ条件で流動性に関す
る安息角及び粘着度の試験を行い、その結果を表Iに示
した。
(8) Using the powder obtained in (7), the angle of repose and the tackiness relating to fluidity were tested under the same conditions as in (2), and the results are shown in Table I.

(9)(7)と同様な操作方法で70%濃度葛根湯末吸着MF
C粉末及び70%濃度葛根湯末吸着軽質無水珪酸粉末を
得た。
(9) 70% concentration Kakkonto powder adsorbed MF by the same operation method as (7)
C powder and 70% concentrated Kakkonto powder adsorbed light anhydrous silicic acid powder were obtained.

(10)(9)で得た粉末を用い(2)と同じ条件で流動性に関す
る安息角及び粘着度の試験を行い、その結果を表Iに示
した。
(10) Using the powder obtained in (9), the angle of repose and the tackiness relating to fluidity were tested under the same conditions as in (2), and the results are shown in Table I.

(11)流動層を用いた70%濃度葛根湯末MFC粉末 吸着性の非常に高い葛根湯末700gを水1,250g
に溶かしこれをスプレー液とする。このスプレー液を流
動層を用いてMFC粉末300gにスプレー吸着させ
る。これで得た粉末を70%葛根湯吸着流動層MFC粉
末とする。同様に軽質無水珪酸に対しても行い70%葛
根湯吸着流動層軽質無水珪酸粉末を得た。
(11) 70% concentration Kakkonto powder MFC powder using a fluidized bed
Dissolve in and use this as the spray liquid. This spray solution is spray-adsorbed on 300 g of MFC powder using a fluidized bed. The powder thus obtained is used as 70% Kakkonto adsorption fluidized bed MFC powder. Similarly, light anhydrous silicic acid was also used to obtain 70% Kakkonto adsorption fluidized bed light anhydrous silicic acid powder.

(12)(11)で得られた粉末に対して(2)と同じ条件で流動
性に関する安息角及び粘着度の試験を行い得た結果を表
Iに示した。
(12) Table I shows the results obtained by subjecting the powder obtained in (11) to the repose angle and the tackiness relating to the fluidity under the same conditions as in (2).

(13)上記の(7),(9)及び(11)で得られた各粉末へ0.5%
(W/W)のステアリン酸マグネシユームを加え、単発
式打錠機木村式KT−II型を用い、すべて同一条件で2
50mgに打錠を行い、各打錠について打錠性の比較試験
を行つた。その結果を表IIに示した。
(13) 0.5% to each powder obtained in (7), (9) and (11) above
(W / W) Magnesium stearate was added and a single-shot tableting machine Kimura KT-II type was used.
Tableting was carried out on 50 mg, and a comparative test of tableting property was carried out for each tableting. The results are shown in Table II.

表Iから50%濃度で、MFCと結晶セルロース末に差
が現われていることが認められる。この差は70%濃度
ではつきりと現れている。粉末として扱える濃度範囲に
MFCと結晶セルロースとの差が明らかに認められる。
MFC末と軽質無水珪酸末との間には粉末として取扱う
上での差異がみられない。
From Table I, it can be seen that a difference appears between MFC and crystalline cellulose powder at a concentration of 50%. This difference clearly appears at the 70% concentration. A difference between MFC and crystalline cellulose is clearly recognized in the concentration range that can be handled as powder.
There is no difference in handling as powder between MFC powder and light anhydrous silicic acid powder.

表IIから、濃度にかかわらず、軽質無水珪酸を用いた場
合、成形性が著しくMFCに比して劣ることが分る。
From Table II, it can be seen that regardless of the concentration, when light anhydrous silicic acid is used, the formability is significantly inferior to that of MFC.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】吸湿性の高い医薬品、化粧品又は食品に微
小繊維状セルロースを添加分散してなる易流動性粉粒体
組成物。
1. A free-flowing powdery or granular material composition obtained by adding and dispersing microfibrous cellulose to a drug, cosmetics or food having high hygroscopicity.
JP60078051A 1985-04-12 1985-04-12 Free-flowing powder composition Expired - Lifetime JPH0617317B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60078051A JPH0617317B2 (en) 1985-04-12 1985-04-12 Free-flowing powder composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60078051A JPH0617317B2 (en) 1985-04-12 1985-04-12 Free-flowing powder composition

Publications (2)

Publication Number Publication Date
JPS61236731A JPS61236731A (en) 1986-10-22
JPH0617317B2 true JPH0617317B2 (en) 1994-03-09

Family

ID=13651048

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60078051A Expired - Lifetime JPH0617317B2 (en) 1985-04-12 1985-04-12 Free-flowing powder composition

Country Status (1)

Country Link
JP (1) JPH0617317B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0829050B2 (en) * 1988-09-21 1996-03-27 正田醤油株式会社 Method for producing non-deliquescent rice snack food
JP4781855B2 (en) * 2006-03-08 2011-09-28 日本メナード化粧品株式会社 Composite powder and makeup cosmetic containing the composite powder
JP2014093946A (en) * 2012-11-07 2014-05-22 Kikkoman Singapore R & D Lab Pte Ltd Method of producing powder soy sauce having solidification preventive effect
EP3135300B1 (en) 2014-04-21 2022-03-30 Daicel Corporation Disintegrating particle composition including microfibrous cellulose
JP6646800B2 (en) * 2015-01-07 2020-02-14 御国色素株式会社 Abrasive slurry containing thickener and method for producing the same
CN110612123A (en) 2017-05-18 2019-12-24 株式会社大赛璐 Composition for disintegrating tablet containing microfibrous cellulose and active ingredient

Also Published As

Publication number Publication date
JPS61236731A (en) 1986-10-22

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