JPH044016B2 - - Google Patents

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Publication number
JPH044016B2
JPH044016B2 JP57187990A JP18799082A JPH044016B2 JP H044016 B2 JPH044016 B2 JP H044016B2 JP 57187990 A JP57187990 A JP 57187990A JP 18799082 A JP18799082 A JP 18799082A JP H044016 B2 JPH044016 B2 JP H044016B2
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Japan
Prior art keywords
starch
water
base material
oil
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.)
Expired - Lifetime
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JP57187990A
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Japanese (ja)
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JPS5976539A (en
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Priority to JP18799082A priority Critical patent/JPS5976539A/en
Publication of JPS5976539A publication Critical patent/JPS5976539A/en
Publication of JPH044016B2 publication Critical patent/JPH044016B2/ja
Granted legal-status Critical Current

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  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Fats And Perfumes (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は液状物質の粉末化用基材に関する。 油脂類や有機溶剤等の液状物質はその用途に応
じて粉末化することが都合よい場合がしばしばあ
り、従来から、食品、医薬、農薬をはじめ、各種
の分野において液状物質の粉末化が試みられてい
る。 一般に、この粉末化は液状物質を粉末化用の基
材に吸着させることにより行なわれ、この基材と
して化工澱粉や天然ガムなどが採用されている。
しかしながら、これら従来の基材は液状物質の吸
着に煩雑な操作が必要であつたり、液状物質の吸
着量が不充分であつたり、吸着させた製品の水膨
潤性が劣るなどの問題があり、液状物質の粉末化
用基材として充分満足するものはなかなか見当ら
ない。 本発明者らは液状物質の粉末化について種々検
討を重ねる間に、意外にも、澱粉またはその誘導
体と、ある種の高分子物質の水分散液をドラムド
ライヤーで乾燥して得られる粉末が液状物質の粉
末化用基材として好適であることを見出し、本発
明を完成するにいたつた。 すなわち、本発明は、澱粉またはその誘導体
と、水溶性もしくは水分散性蛋白質、および水溶
性合成高分子からなる群から選ばれる1種または
2種以上の高分子物質との水分散液の、8.2〜20
ml/gの水溶性を有するドラムドライヤー乾燥粉
末からなる液状物質の粉末化用基材を提供するも
のである。本発明の基材は嵩高く、比容積が大き
く、高い液状物質吸着能を示し、かつ、強度の高
い粉末で、単に液状物質と混合するのみで大量の
液状物質を吸着し、その高い強度から、吸着工程
やその後の保持、輸送時にもいわゆる液漏れをほ
とんど起すことがない。しかも、得られた液状物
質粉末化製品はすぐれた水膨潤性を示すという利
点も有する。 かくして、本発明で用いる澱粉またはその誘導
体としては、馬鈴薯澱粉、トウモロコシ澱粉、モ
チトウモロコシ澱粉、甘藷澱粉、小麦澱粉、米澱
粉、タピオカ澱粉、サゴ澱粉等から選ばれる天然
澱粉、アミロースやアミロペクチン分画物、エー
テル化澱粉、エステル化澱粉、酸化澱粉、酸処理
化澱粉、グラフト化澱粉等から選ばれる化工澱粉
が挙げられる。 該高分子物質としては、ゼラチン、カゼインナ
トリウム、水溶性卵白、全卵、にかわ、コラーゲ
ンなどの水溶性もしくは水分散蛋白質、ポリビニ
ルアルコール、ポリアクリル酸ナトリウム、ポリ
エチレンオキサイドなどの水溶性合成高分子が用
いられる。これらの高分子物質は単独でも、2種
以上を併用してもよく、その使用量は所望の粉末
化製品の性能に応じて適宜選択できるが、通常、
用いる澱粉またはその誘導体に対して0.1〜10%
(重量%、以下同じ)程度が好ましい。ことに、
高分子物質として水溶性もしくは水分散性蛋白質
を用いることが好ましい。 本発明の基材は澱粉またはその誘導体と高分子
物質を含有する水分散液を調製し、常法に従つ
て、ダブル式あるいはシングル式のドラムドライ
ヤーで乾燥、粉末化することにより製造できる。 該水分散液中の澱粉またはその誘導体の濃度は
実際のドラムドライヤーの運転条件に応じて適宜
選択でき、通常、30〜60%とすることが好まし
い。また、ドラムドライヤーの運転条件には特に
制約はなく、通常の温度、圧力、回転数、ロール
スリツト巾が採用でき、使用原料や粉末化製品の
性能、用途に応じて適宜調整する。 なお、該水分散液にグリセリン脂肪酸エステ
ル、シヨ糖脂肪酸エステル、プロピレングリコー
ル脂肪酸エステル、ソルビタン脂肪酸エステル、
脂肪酸塩、アルキル硫酸エステル、アルキルベン
ゼンスルホン酸塩、アルキルアミン塩、第4級ア
ンモニウム塩、アルキルベタイン、レシチン等の
界面活性剤を澱粉またはその誘導体に対して0.01
〜10%添加してもよく、これにより、得られる粉
末の強度、水膨潤性をさらに向上させることがで
きる。 得られた乾燥粉末は常法により篩別機により粒
度を調整する。通常、20〜100メツシユ程度の粒
度が好ましい。 かくして得られた本発明の液状物質粉末化用基
材は、通常、8.2〜20ml/gの比容積を有し、食
品、医薬、農薬をはじめ、各種の工業分野におい
て粉末化の要求される液状物質の粉末化に好適に
使用できる。かかる液状物質としては、例えば、
ナタネ油、ゴマ油、大豆油、落花生油、綿実油、
コーン油、サフラワー油、ヤシ油、パーム油、ヒ
マシ油、ラード、ヘツド、魚油、鯨油、石油、ワ
セリン、バター、マーガリン、硬化油、シヨート
ニング、肝油、香油、香辛油等の油脂類、メタノ
ール、エタノール、イソプロパノール、グリセリ
ン等のアルコール類、アセトン、エチレングリコ
ール、プロピレングリコール、キシレン、トルエ
ン等の溶剤、各種農薬乳剤などが挙げられ、これ
らを、ニーダー、ブレンダー、エアーミツクス等
の混合機により本発明の基材と混合し、吸着させ
るだけで粉末化することができる。 つぎに実施例を挙げて本発明をさらに詳しく説
明する。なお、実施例中、「部」とあるは、いず
れも重量部を意味する。 実施例 1 ヒドロキシプロピルスターチ(置換度0.05)
100部を水に分散させてボーメ度15度に調整し、
これにゼラチン1部を水4部に溶解したゼラチン
水溶液、モノグリセリンエステル0.1部を加え、
均一に混合した。この分散液を実施例1と同様に
ダブルドラムドライヤーで糊化、乾燥粉末化し、
24メツシユの篩に通し、比容積9.2ml/gの液状
物質の粉末化用基材を得た。 実施例 2 澱粉リン酸エステルナトリウム(置換度0.05)
100部を水に分散させてボーメ度15度に調整し、
これに乾燥卵白1部を水7部に溶解した卵白水溶
液を加え、均一に混合した。この分散液を実施例
1と同様に、ダブルドラムドライヤーで糊化、乾
燥粉末化し、24メツシユの篩に通し、比容積9.5
ml/gの液状物質の粉末化用基材を得た。 実施例 3 モチトウモロコシ澱粉100部を水に分散させて
ボーメ度18度に調整し、これに乾燥卵白1部を水
7部に溶解した卵白水溶液を加え、均一に混合し
た。この分散液を実施例1と同様に、ダブルドラ
ムドライヤーで糊化、乾燥粉末化し、24メツシユ
の篩に通し、比容積11.2ml/gの液状物質の粉末
化用基材を得た。 対照例 1 モチトウモロコシ澱粉100部を水に分散させて
ボーメ度18度に調整した。この分散液を実施例1
と同様に、ダブルドラムドライヤーで糊化、乾燥
粉末化し、24メツシユの篩に通し、比容積4.2
ml/gの液状物質の粉末化用基材を得た。 これらの実施例および対照例で得た基材の性能
をつぎのように試験した。 試験−1 各基材の試料100gを小型ブレンダー(回転数
60r.p.m.)で10分間混合し、混合前後の比容積お
よび吸油量を測定し、耐破壊強度を試験した。 吸油量の測定はJIS K5101−196419の方法に従
い、つぎのとおり行なつた。 試料3gをガラス板にとり、煮アマニ油をビユ
レツトから少量づつ試料の中央に滴下し、自然に
吸油するのを待ち、再度滴下する操作をくり返
し、全体がバテ状になるまで滴下をつづけた。使
用した煮アマニ油の量から次式により吸油量Gを
算出した。 G(%)=H/S×100 H:煮アマニ油量(ml) S:試料重量(g) 結果を第1表に示す。なお、各試料の混合、破
壊による比容積および吸油量の減少を比較するた
め次式に従つて算出した残存率も示す。 残存率(%)=混合後の数値/混合前の数値×10
0
The present invention relates to a substrate for powdering liquid substances. It is often convenient to pulverize liquid substances such as oils and fats and organic solvents depending on their use, and attempts have been made to pulverize liquid substances in various fields including food, medicine, and agricultural chemicals. ing. Generally, this powdering is carried out by adsorbing the liquid substance onto a powdering base material, and modified starch, natural gum, etc. are used as the base material.
However, these conventional base materials have problems such as requiring complicated operations to adsorb liquid substances, insufficient adsorption amount of liquid substances, and poor water swelling properties of adsorbed products. It is difficult to find a material that is fully satisfactory as a base material for powdering liquid substances. While the present inventors conducted various studies on powdering liquid substances, they unexpectedly found that a powder obtained by drying an aqueous dispersion of starch or its derivatives and a certain type of polymer substance using a drum dryer was found to be a liquid substance. It was discovered that it is suitable as a base material for powdering substances, and the present invention was completed. That is, the present invention provides an aqueous dispersion of starch or a derivative thereof and one or more polymeric substances selected from the group consisting of water-soluble or water-dispersible proteins and water-soluble synthetic polymers. ~20
The present invention provides a base material for powdering a liquid substance consisting of a drum dryer dry powder having a water solubility of ml/g. The base material of the present invention is a powder that is bulky, has a large specific volume, shows high liquid substance adsorption ability, and has high strength. , so-called liquid leakage hardly occurs during the adsorption process, subsequent holding, and transportation. Moreover, the resulting powdered liquid material product also has the advantage of exhibiting excellent water swelling properties. Thus, the starch or its derivatives used in the present invention include natural starches selected from potato starch, corn starch, waxy corn starch, sweet potato starch, wheat starch, rice starch, tapioca starch, sago starch, and amylose and amylopectin fractions. , etherified starch, esterified starch, oxidized starch, acid-treated starch, grafted starch, and the like. As the polymer substance, water-soluble or water-dispersible proteins such as gelatin, sodium caseinate, water-soluble egg white, whole egg, glue, and collagen, and water-soluble synthetic polymers such as polyvinyl alcohol, sodium polyacrylate, and polyethylene oxide are used. It will be done. These polymeric substances may be used alone or in combination of two or more, and the amount used can be selected as appropriate depending on the performance of the desired powdered product.
0.1-10% based on the starch or its derivative used
(% by weight, the same applies hereinafter) is preferable. In particular,
It is preferable to use water-soluble or water-dispersible proteins as the polymeric substance. The base material of the present invention can be produced by preparing an aqueous dispersion containing starch or a derivative thereof and a polymeric substance, and drying and pulverizing the dispersion using a double or single drum dryer according to a conventional method. The concentration of starch or its derivative in the aqueous dispersion can be appropriately selected depending on the actual operating conditions of the drum dryer, and is usually preferably 30 to 60%. Further, there are no particular restrictions on the operating conditions of the drum dryer, and normal temperatures, pressures, rotational speeds, and roll slit widths can be used, and are adjusted as appropriate depending on the raw materials used, the performance of the powdered product, and the intended use. In addition, the aqueous dispersion contains glycerin fatty acid ester, sucrose fatty acid ester, propylene glycol fatty acid ester, sorbitan fatty acid ester,
Surfactants such as fatty acid salts, alkyl sulfate esters, alkylbenzene sulfonates, alkyl amine salts, quaternary ammonium salts, alkyl betaines, and lecithin are added to starch or its derivatives at a rate of 0.01
It may be added in an amount of up to 10%, thereby further improving the strength and water swelling properties of the resulting powder. The particle size of the obtained dry powder is adjusted using a sieve in a conventional manner. Usually, a particle size of about 20 to 100 mesh is preferred. The thus obtained base material for powdering a liquid substance of the present invention usually has a specific volume of 8.2 to 20 ml/g, and is suitable for use in liquid substances that are required to be powdered in various industrial fields including food, medicine, and agricultural chemicals. It can be suitably used for powdering substances. Such liquid substances include, for example,
rapeseed oil, sesame oil, soybean oil, peanut oil, cottonseed oil,
Oils and fats such as corn oil, safflower oil, coconut oil, palm oil, castor oil, lard, head, fish oil, whale oil, petroleum, vaseline, butter, margarine, hydrogenated oil, shell toning, cod liver oil, perfume oil, spice oil, methanol, Examples include alcohols such as ethanol, isopropanol, and glycerin, solvents such as acetone, ethylene glycol, propylene glycol, xylene, and toluene, and various pesticide emulsions. It can be turned into powder simply by mixing it with other materials and adsorbing it. Next, the present invention will be explained in more detail with reference to Examples. In addition, in the examples, all "parts" mean parts by weight. Example 1 Hydroxypropyl starch (degree of substitution 0.05)
Disperse 100 parts in water and adjust the Baume degree to 15 degrees,
To this, add an aqueous gelatin solution prepared by dissolving 1 part of gelatin in 4 parts of water, and 0.1 part of monoglycerin ester.
Mixed evenly. This dispersion was gelatinized and dried into powder using a double drum dryer in the same manner as in Example 1.
The mixture was passed through a 24-mesh sieve to obtain a base material for powdering a liquid substance with a specific volume of 9.2 ml/g. Example 2 Sodium starch phosphate (degree of substitution 0.05)
Disperse 100 parts in water and adjust the Baume degree to 15 degrees,
An aqueous egg white solution prepared by dissolving 1 part of dried egg white in 7 parts of water was added to this and mixed uniformly. As in Example 1, this dispersion was gelatinized using a double drum dryer, dried and powdered, passed through a 24-mesh sieve, and the specific volume was 9.5.
A base material for powdering a liquid substance of ml/g was obtained. Example 3 100 parts of waxy corn starch was dispersed in water and adjusted to a Baume degree of 18 degrees, and an aqueous egg white solution prepared by dissolving 1 part of dried egg white in 7 parts of water was added thereto and mixed uniformly. This dispersion was gelatinized and dried into a powder using a double drum dryer in the same manner as in Example 1, and passed through a 24-mesh sieve to obtain a base material for powdering a liquid substance with a specific volume of 11.2 ml/g. Control Example 1 100 parts of waxy corn starch was dispersed in water and adjusted to a Baume degree of 18 degrees. This dispersion was prepared in Example 1.
Similarly, gelatinize with a double drum dryer, dry powder, pass through a 24-mesh sieve, and reduce the specific volume to 4.2.
A base material for powdering a liquid substance of ml/g was obtained. The performance of the substrates obtained in these Examples and Control Examples was tested as follows. Test-1 100g of each base material sample was placed in a small blender (rotation speed
60 rpm) for 10 minutes, the specific volume and oil absorption before and after mixing were measured, and the fracture resistance strength was tested. The oil absorption was measured in accordance with the method of JIS K5101-196419 as follows. 3 g of the sample was placed on a glass plate, and boiled linseed oil was dripped into the center of the sample in small amounts from a biuret, waiting for the oil to be naturally absorbed, and the operation of dropping again was repeated until the entire sample became sticky. Oil absorption amount G was calculated from the amount of boiled linseed oil used using the following formula. G (%) = H/S x 100 H: Boiled flaxseed oil amount (ml) S: Sample weight (g) The results are shown in Table 1. In addition, in order to compare the reduction in specific volume and oil absorption due to mixing and destruction of each sample, the residual ratio calculated according to the following formula is also shown. Survival rate (%) = Value after mixing / Value before mixing × 10
0

【表】 第1表に示すごとく、本発明の基材は対照例の
ものよりきわめて比容積、吸油量が大きく、か
つ、高い耐破壊性を有している。なお、これらの
実施例で用いた澱粉および澱粉誘導体自体を用い
て同様に試験したところ、混合前、混合後共に、
比容積2.2〜2.4ml/g、吸油量60〜64%であつ
た。 試験−2 各基材の試験20gにナタネ油15gを吸着させ、
予め重量を秤量した200cm2の紙(厚さ3mm)上
に100cm2の面積で広げ、100cm2当り、20Kgの荷重を
加え、1日放置した。紙に吸着されたナタネ油
量を秤量し、次式により基材に吸着されたナタネ
油の荷重圧縮による残存率を算出した。 残存率(%)=15−紙に吸着されたナタネ油(g)/
15×100 結果を第2表に示す。
[Table] As shown in Table 1, the base material of the present invention has a much larger specific volume and oil absorption than the control example, and has high fracture resistance. In addition, when similar tests were conducted using the starch and starch derivative itself used in these Examples, both before and after mixing,
The specific volume was 2.2 to 2.4 ml/g and the oil absorption was 60 to 64%. Test-2 15g of rapeseed oil was adsorbed on 20g of each base material,
It was spread over an area of 100 cm 2 on a 200 cm 2 paper (thickness 3 mm) that had been weighed in advance, and a load of 20 kg was applied per 100 cm 2 and left for one day. The amount of rapeseed oil adsorbed on the paper was weighed, and the residual rate of rapeseed oil adsorbed on the substrate under load compression was calculated using the following formula. Residual rate (%) = 15 - rapeseed oil adsorbed on paper (g) /
15×100 The results are shown in Table 2.

【表】 第2表の結果からも本発明の基材がすぐれた強
度および吸油能を有することが明らかである。な
お、これらの実施例で用いた澱粉および澱粉誘導
体自体を用いて同様に試験したところ、残存率は
いずれも約28%であつた。
[Table] It is clear from the results in Table 2 that the base material of the present invention has excellent strength and oil absorption ability. In addition, when the starch and starch derivative itself used in these Examples were similarly tested, the residual rate was about 28% in both cases.

Claims (1)

【特許請求の範囲】 1 馬鈴薯澱粉、トウモロコシ澱粉、モチトウモ
ロコシ澱粉、甘藷澱粉、小麦澱粉、米澱粉、タピ
オカ澱粉、サゴ澱粉、アミロース、アミロペクチ
ン分画物、エーテル化澱粉、エステル化澱粉、酸
化澱粉、酸処理化澱粉およびグラフト化澱粉から
なる群から選ばれる澱粉またはその誘導体と、 水溶性もしくは水分散性蛋白質および水溶性合
成高分子からなる群から選ばれる1種または2種
以上の高分子物質との水分散液の、8.2〜20ml/
gの比容積を有するドラムドライヤー乾燥粉末か
らなることを特徴とする液状物質の粉末化用基
材。 2 該高分子物質が水溶性もしくは水分散性蛋白
質である前記第1項の基材。 3 澱粉またはその誘導体に対して0.1〜10重量
%の該高分子物質を含有する前記第1項または第
2項の基材。
[Scope of Claims] 1 Potato starch, corn starch, waxy corn starch, sweet potato starch, wheat starch, rice starch, tapioca starch, sago starch, amylose, amylopectin fraction, etherified starch, esterified starch, oxidized starch, Starch or a derivative thereof selected from the group consisting of acid-treated starch and grafted starch; and one or more polymeric substances selected from the group consisting of water-soluble or water-dispersible proteins and water-soluble synthetic polymers. of aqueous dispersion, 8.2 to 20 ml/
A base material for powdering a liquid substance, characterized in that it consists of a drum dryer-dried powder having a specific volume of g. 2. The base material of item 1 above, wherein the polymeric substance is a water-soluble or water-dispersible protein. 3. The base material according to item 1 or 2 above, which contains 0.1 to 10% by weight of the polymeric substance based on starch or its derivative.
JP18799082A 1982-10-25 1982-10-25 Base material for pulverizing liquid material Granted JPS5976539A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18799082A JPS5976539A (en) 1982-10-25 1982-10-25 Base material for pulverizing liquid material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18799082A JPS5976539A (en) 1982-10-25 1982-10-25 Base material for pulverizing liquid material

Publications (2)

Publication Number Publication Date
JPS5976539A JPS5976539A (en) 1984-05-01
JPH044016B2 true JPH044016B2 (en) 1992-01-27

Family

ID=16215687

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18799082A Granted JPS5976539A (en) 1982-10-25 1982-10-25 Base material for pulverizing liquid material

Country Status (1)

Country Link
JP (1) JPS5976539A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10168593A (en) * 1996-12-12 1998-06-23 Teikoku Piston Ring Co Ltd Chromium alloy plating coating, plating method therefor and member having this coating

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5059577A (en) * 1986-09-12 1991-10-22 Hatton John H Fluid absorbent composition
US5021390A (en) * 1986-09-12 1991-06-04 Hatton John H Liquid hydrocarbon absorbent composition and method
JP5216979B2 (en) * 2007-12-05 2013-06-19 日本食品化工株式会社 desiccant

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5233893A (en) * 1975-09-11 1977-03-15 Seiwa Kasei Kk Method of producing adsorbent

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5233893A (en) * 1975-09-11 1977-03-15 Seiwa Kasei Kk Method of producing adsorbent

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10168593A (en) * 1996-12-12 1998-06-23 Teikoku Piston Ring Co Ltd Chromium alloy plating coating, plating method therefor and member having this coating

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JPS5976539A (en) 1984-05-01

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