JPS6152740B2 - - Google Patents

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Publication number
JPS6152740B2
JPS6152740B2 JP57187989A JP18798982A JPS6152740B2 JP S6152740 B2 JPS6152740 B2 JP S6152740B2 JP 57187989 A JP57187989 A JP 57187989A JP 18798982 A JP18798982 A JP 18798982A JP S6152740 B2 JPS6152740 B2 JP S6152740B2
Authority
JP
Japan
Prior art keywords
water
base material
starch hydrolyzate
oil
mucilage
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
Application number
JP57187989A
Other languages
Japanese (ja)
Other versions
JPS5976538A (en
Inventor
Yasuo Endo
Akira Myazaki
Katsumi Suzuki
Shigeki Kio
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.)
Nippon Starch Chemical Co Ltd
Original Assignee
Nippon Starch Chemical 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 Nippon Starch Chemical Co Ltd filed Critical Nippon Starch Chemical Co Ltd
Priority to JP57187989A priority Critical patent/JPS5976538A/en
Publication of JPS5976538A publication Critical patent/JPS5976538A/en
Publication of JPS6152740B2 publication Critical patent/JPS6152740B2/ja
Granted legal-status Critical Current

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  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Fats And Perfumes (AREA)
  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • Edible Oils And Fats (AREA)

Description

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

本発明は液状物質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
して種々の物質が採用されている。しかしなが
ら、液状物質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、澱粉加水分解物の水
溶液中にある種の高分子物質を存在させ、ドラム
ドライヤーで乾燥して得られる粉末が液状物質粉
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、澱粉加水分解物と、海藻
抽出物、植物性種子粘質物、植物性果実粘質物、
植物性樹脂様粘質物、微生物産生粘質物、水溶性
もしくは水分散性蛋白質、セルロース誘導体およ
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のドラムドライヤー
乾燥粉末からなる液状物質粉末化用基材を提供す
るものである。 従来から、澱粉加水分解物の水溶液をドラムド
ライヤーで乾燥して得られる粉末を液状物質粉末
化用基材として用いることが提案されているが
(特開昭53−23305号)、単に澱粉加水分解物水溶
液をドラムドライヤーで乾燥しても、嵩高い比容
積の大きい、比較的高い液状物質吸着能を示す粉
末が得られるものの、この粉末が脆弱なために液
状物質の吸着工程やその後の保存、輸送時に粉末
が破壊され、いわゆる液漏れを生じやすい欠点が
ある。また、ドラムドライヤー乾燥上の技術的制
約から、用いる澱粉加水分解物はDE(デキスト
ロース当量)18以下のものに制限され、そのため
に液状物質を吸着させて得られる製品の水溶性が
劣り、水溶性の良好な製品が得がたい欠点があ
る。これに対し、本発明によれば、高分子物質を
用いることにより、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
が得られ、しかも、約30までの高いDEを有する
澱粉加水分解物を用いても支障なくドラムドライ
ヤー乾燥が行なえ、液漏れなどの欠点のない、水
溶性の向上した製品が得られる。 かくして、本発明で用いる澱粉加水分解物は、
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、サゴ澱粉等の天然澱粉、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、架橋澱粉、酸化澱粉、酸処理化澱粉、グラ
フト化澱粉等の化工澱粉などの各種の澱粉および
その誘導体を常法に従つて酸分解、アルカリ分
解、酵素分解またはそれらの組合せによつて加水
分解したものでよく、乾燥粉末化の観点から、
DE約30以下、通常、DE約5〜30のものが好まし
く、特に、液状物質を吸着させた製品の水溶性向
上の観点から、DE約20〜30のものが好ましい。
なお、ここでいうDEとは無水固形分中の還元糖
の比で、還元糖量は東京大学農芸化学教室編、実
験農芸化学、改訂版、下巻、638〜639頁および附
表第3表(昭和38年、朝倉書店発行)に記載に従
つてフエーリング・レーマン・シヨール法により
測定したものである。 該高分子物質としては、アルギン酸ナトリウ
ム、寒天、カラギーナン、フアーセランなどの海
藻抽出物、ローカストビーンガム、グアーガム、
タマリンドのような植物性種子粘質物、ペクチン
のような植物性果実粘質物、アラビアガム、トラ
ガントガム、カラヤガム、ガツテイーガムなどの
植物性樹脂様粘質物、デキストラン、キサンタン
ガム、プルラン、カードランなどの微生物産生粘
質物、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
くは水分散性蛋白質、カルボキシメチルセルロー
ス、メチルセルロース、ヒドロキシエチルセルロ
ース、ヒドロキシプロピルセルロースなどのセル
ロース誘導体、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加水分解物と該高分子物質
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加水分解物の濃度は実際の
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0.01〜0.5%、また、さらに、所望
により、前記のような澱粉またはその誘導体を
0.1〜10%程度添加してもよく、これにより、得
られる粉末の強度、液状物質を吸着させた場合の
水溶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、4〜20ml/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。 つぎに調整例および吸着を挙げて本発明をさら
に詳しく説明する。なお、調製例、実施例中、
「部」とあるは、いずれも重量部を意味する。 調整例 1 馬鈴薯澱粉100部を水に分散させてボーメ度20
度の分散液を調整し、α―アミラーゼ(酵素力価
13000U/g)0.05〜0.5部を加え、85〜90℃で20〜
120分間加水分解した。ついで、稀塩酸でpH4.0
として酵素を失活させた後、炭酸カルシウムで
pH5.5に調整して、各々、DE10.5、17.8および
20.2の澱粉加水分解物溶液を得た。 調製例 2 馬鈴薯澱粉100部を水に分散させてボーメ度20
度の分散液を調製し、α―アミラーゼ(酵素力価
13000U/g)0.07部を加え、85〜90℃で40分間加
水分解した後、60℃に冷却し、さらにβ―アミラ
ーゼ(酵素力価3000U/g)0.2〜0.3部を加え、60
〜240分間加水分解した。ついで、稀塩酸で
pH4.0とし、95℃まで加熱し、酵素を失活させ、
炭酸カルシウムでpH5.5に調整して、各々、
DE29.5および33.2の澱粉加水分解物溶液を得
た。 実施例 1 調製例1および2で得られた澱粉加水分解物の
溶液を精製、濃縮し、濃度50%の澱粉加水分解物
水溶液とし、その200部に予め溶解したゼラチン
0.3部を加え、混合、溶解した。この溶液を常法
に従つてダブルドラムドライヤー(蒸気内圧:
5.5Kg/cm2、ドラム径:1.2m、回転数:0.85r.p.m.
)で乾燥粉末化し、各々、第1表に示すごとき比
容積を有する液状物質粉末化用基材を得た。
The present invention relates to a substrate for powdering a liquid substance. 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 various substances are employed as this base material. However, it is difficult to find a material that is fully satisfactory as a base material for powdering a liquid substance. While conducting various studies on powdering liquid substances, the present inventors unexpectedly discovered that a powder obtained by adding a certain type of polymer substance to an aqueous solution of starch hydrolyzate and drying it with a drum dryer. It was discovered that it is suitable as a base material for powdering a liquid substance, and the present invention was completed. That is, the present invention provides a starch hydrolyzate, a seaweed extract, a vegetable seed mucilage, a vegetable fruit mucilage,
A drum dryer-dried powder of one or more polymeric substances selected from the group consisting of vegetable resin-like mucilage, microbial-produced mucilage, water-soluble or water-dispersible proteins, cellulose derivatives, and water-soluble synthetic polymers. The present invention provides a base material for powdering a liquid substance. Conventionally, it has been proposed to use a powder obtained by drying an aqueous solution of starch hydrolyzate with a drum dryer as a base material for powdering a liquid substance (Japanese Patent Application Laid-open No. 53-23305), Even if an aqueous solution is dried using a drum dryer, a bulky powder with a large specific volume and a relatively high ability to adsorb liquid substances can be obtained. The disadvantage is that the powder is easily destroyed during transportation, resulting in so-called liquid leakage. In addition, due to technical constraints in drying with a drum dryer, the starch hydrolyzate used is limited to DE (dextrose equivalent) of 18 or less, which results in poor water solubility of products obtained by adsorbing liquid substances; Although it is a good product, it has some drawbacks that make it difficult to obtain. In contrast, according to the present invention, by using a polymeric substance, a powder that is bulky, has a large specific volume, exhibits high liquid substance adsorption ability, and has high strength can be obtained. Even if a starch hydrolyzate with a high DE is used, it can be dried using a drum dryer without any problems, and a product with improved water solubility without defects such as leakage can be obtained. Thus, the starch hydrolyzate used in the present invention is
Natural starches such as potato starch, corn starch, waxy corn starch, sweet potato starch, wheat starch, rice starch, tapioca starch, sago starch, amylose and amylopectin fractions, etherified starch, esterified starch, cross-linked starch, oxidized starch, Various starches such as acid-treated starches, modified starches such as grafted starches, and their derivatives may be hydrolyzed by acid decomposition, alkali decomposition, enzymatic decomposition, or a combination thereof according to conventional methods, and dry powders may be used. From the perspective of
A DE of about 30 or less, usually a DE of about 5 to 30 is preferred, and a DE of about 20 to 30 is particularly preferred from the viewpoint of improving the water solubility of a product to which a liquid substance is adsorbed.
Note that DE here refers to the ratio of reducing sugar in the anhydrous solid content, and the amount of reducing sugar is determined from the University of Tokyo, Department of Agricultural Chemistry, Experimental Agricultural Chemistry, Revised Edition, Volume 2, pp. 638-639 and Appendix Table 3 ( It was measured by the Fehring-Lehmann-Schill method according to the description in 1963, published by Asakura Shoten). Examples of the polymeric substances include sodium alginate, agar, carrageenan, seaweed extracts such as furcelan, locust bean gum, guar gum,
Vegetable seed mucilage such as tamarind, vegetable fruit mucilage such as pectin, vegetable resin-like mucilage such as gum arabic, gum tragacanth, gum karaya, and gum gatuti, microorganism-produced mucilage such as dextran, xanthan gum, pullulan, and curdlan. water-soluble or water-dispersible proteins such as gelatin, sodium caseinate, water-soluble egg white, whole eggs, glue, collagen, cellulose derivatives such as carboxymethyl cellulose, methyl cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose, polyvinyl alcohol, sodium polyacrylate , water-soluble synthetic polymers such as polyethylene oxide are used. These polymeric substances may be used alone or in combination of two or more,
The amount used can be appropriately selected depending on the performance of the desired powdered product, but it is usually preferably about 0.1 to 10% (wt%, same hereinafter) based on the starch or derivative thereof used. 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 a starch hydrolyzate and the polymeric substance, and drying and pulverizing the dispersion using a double or single drum dryer according to a conventional method. The concentration of the starch hydrolyzate 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%. In addition, 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 the performance of the raw materials and powdered products
Adjust as appropriate depending on the purpose. In addition, the aqueous dispersion contains glycerin fatty acid ester, sucrose fatty acid ester, propylene glycol fatty acid ester, sorbitan fatty acid ester,
0.01 to 0.5% of surfactants such as fatty acid salts, alkyl sulfate esters, alkylbenzene sulfonates, alkyl amine salts, quaternary ammonium salts, alkyl betaines, lecithin, and, if desired, starch or its derivative
It may be added in an amount of about 0.1 to 10%, thereby further improving the strength of the powder obtained and the water solubility when a liquid substance is adsorbed. 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 4 to 20 ml/g, and is suitable for liquid substances that are required to be powdered in various industrial fields including foods, medicines, 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 agrochemical emulsions.These may be mixed into the base material of the present invention using a mixer such as a kneader, blender, or air mixer. It can be powdered simply by mixing it with and adsorbing it. Next, the present invention will be explained in more detail by giving examples of adjustment and adsorption. In addition, in the preparation examples and examples,
All references to "parts" mean parts by weight. Adjustment example 1 Disperse 100 parts of potato starch in water to obtain Baume degree of 20
α-Amylase (enzyme titer)
13000U/g) Add 0.05~0.5 parts and heat at 85~90℃ for 20~
Hydrolyzed for 120 minutes. Then, adjust the pH to 4.0 with dilute hydrochloric acid.
After deactivating the enzyme as
Adjusted to pH5.5, DE10.5, 17.8 and
A starch hydrolyzate solution of 20.2 was obtained. Preparation Example 2 Disperse 100 parts of potato starch in water to obtain a Baume degree of 20
Prepare a dispersion of α-amylase (enzyme titer).
Add 0.07 parts of β-amylase (enzyme titer 3000 U/g), hydrolyze at 85-90°C for 40 minutes, cool to 60°C, add 0.2-0.3 parts of β-amylase (enzyme titer 3000 U/g), and hydrolyze at 85-90°C for 40 minutes.
Hydrolyzed for ~240 minutes. Then, with dilute hydrochloric acid
Adjust the pH to 4.0 and heat to 95℃ to inactivate the enzyme.
Adjust the pH to 5.5 with calcium carbonate, and
Starch hydrolyzate solutions with DE 29.5 and 33.2 were obtained. Example 1 The starch hydrolyzate solutions obtained in Preparation Examples 1 and 2 were purified and concentrated to obtain a starch hydrolyzate aqueous solution with a concentration of 50%, and 200 parts of the starch hydrolyzate solution was added with pre-dissolved gelatin.
0.3 part was added, mixed and dissolved. This solution was dried using a double drum dryer (steam internal pressure:
5.5Kg/cm 2 , drum diameter: 1.2m, rotation speed: 0.85rpm
) to obtain substrates for powdering liquid substances having specific volumes as shown in Table 1.

【表】 実施例 2 調製例1で得たDE20.2の澱粉加水分解物の50
%水溶液200部に、グアーガム0.5部を予め水25部
で糊化させて添加し、均一に混合した。この溶液
を実施例1と同様にドラムドライヤーで乾燥、粉
末化し、24メツシユの篩に通し、比容積13.5ml/
gの液状物質粉末化用基材(試料番号6)を得
た。 実施例 3 調製例2で得たDE29.5の澱粉加水分解物の50
%水溶液200部に全卵1部を加え、均一に混合し
た。この溶液を実施例1と同様にドラムドライヤ
ーで乾燥、粉末化し、24メツシユの篩に通し、比
容積11.4ml/gの液状物質粉末化用基材(試料番
号7)を得た。 対照例 調製例1および2で得られたDE10.5、17.8、
20.2および29.5の樹脂加水分解物の50%水溶液を
実施例1と同様にドラムドライヤーで乾燥、粉末
化し、第2表に示す液状物質粉末化用基材を得
た。
[Table] Example 2 Starch hydrolyzate of DE20.2 obtained in Preparation Example 1
% aqueous solution, 0.5 part of guar gum was previously gelatinized with 25 parts of water and mixed uniformly. This solution was dried and powdered using a drum dryer in the same manner as in Example 1, passed through a 24-mesh sieve, and the specific volume was 13.5 ml/
A base material for powdering a liquid substance (sample number 6) was obtained. Example 3 50% of starch hydrolyzate with DE29.5 obtained in Preparation Example 2
1 part of whole egg was added to 200 parts of % aqueous solution and mixed uniformly. This solution was dried and powdered using a drum dryer in the same manner as in Example 1, and passed through a 24-mesh sieve to obtain a substrate for powdering a liquid substance (sample number 7) with a specific volume of 11.4 ml/g. Control example DE10.5, 17.8, obtained in Preparation Examples 1 and 2
50% aqueous solutions of the resin hydrolysates of 20.2 and 29.5 were dried and powdered using a drum dryer in the same manner as in Example 1 to obtain substrates for powdering liquid substances shown in Table 2.

【表】 なお、DE33.2のものは高分子物質の非存在下
では乾燥できなかつた。 これらの実施例および対照例で得られた基材の
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
吸油するのを持ち、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3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×100
[Table] In addition, those with DE33.2 could not be dried in the absence of polymeric substances. 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 in small amounts at the center of the sample from a biuret, held so that it would naturally absorb the oil, and the process of dropping again was repeated until the entire sample became batter-like. Oil absorption amount G was calculated from the amount of boiled linseed oil used using the following formula. G (%)=H/S×100 H: Boiled linseed oil amount (ml) S: Sample weight (g) The results are shown in Table 3. 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 × 100

【表】 第3表に示すごとく、本発明の基材(試料番号
1〜7)は対照例のもの(試料番号8〜11)に比
較して耐破壊性が非常に高く(なお、試料番号
5,10,11が高い残存率を示すのはその組織がア
メ状を呈していることによるものと考えられ
る)、また、ことに高いDEにおいて対照例のもの
に比し、10倍以上の吸油量を有する。 試験―2 (1) ビーカーに水100mlを入れ、これに各試料2
gを投入し、自然に吸水してビーカー底に完全
に沈降するまでの時間を測定した(沈降が早い
方が水溶性、水分散性が良好)。 (2) 各試料2gにナタネ油2gを吸着させ、(1)と
同様に水に投入し、自然に吸水させ、油を完全
に放出するまでの時間を測定した(油の放出の
早い方が水溶性、水分散性が良好)。 結果を第4表に示す。
[Table] As shown in Table 3, the base materials of the present invention (sample numbers 1 to 7) have extremely high fracture resistance compared to the control examples (sample numbers 8 to 11) (sample numbers The reason why 5, 10, and 11 show a high survival rate is thought to be due to their candy-like structure), and especially at high DE, the oil absorption is more than 10 times that of the control example. have a quantity. Test-2 (1) Put 100ml of water in a beaker and add each sample 2 to it.
g was added, and the time taken for it to naturally absorb water and completely settle to the bottom of the beaker was measured (the faster the sedimentation, the better the water solubility and water dispersibility). (2) 2 g of rapeseed oil was adsorbed on 2 g of each sample, and the samples were poured into water in the same manner as in (1), allowed to absorb water naturally, and the time taken until the oil was completely released was measured (the faster the oil release (Good water solubility and water dispersibility). The results are shown in Table 4.

【表】【table】

【表】 第4表に示すごとく、本発明の基材は対照例の
基材(試料番号8および9)に比べ、水溶性、水
分散性がすぐれている。なお、試料番号10および
11のものはアメ状を呈し、試験―2(1)に供し得な
かつた。また、試験―2(2)においてナタネ油をほ
とんど吸着しなかつた。
[Table] As shown in Table 4, the base material of the present invention has better water solubility and water dispersibility than the base materials of control examples (sample numbers 8 and 9). In addition, sample number 10 and
Sample No. 11 had a candy-like appearance and could not be subjected to Test-2 (1). Also, in Test-2 (2), almost no rapeseed oil was adsorbed.

Claims (1)

【特許請求の範囲】 1 澱粉加水分解物と、海藻抽出物、植物性種子
粘質物、植物性果実粘質物、植物性樹脂様粘質
物、微生物生生粘質物、水溶性もしくは水分散性
蛋白質、セルロース誘導体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
高分子物質の水分散液の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粉末化用基
材。 2 澱粉加水分解物がDE(テキストロース当
量)約30以下のものである前記第1項の基材。 3 澱粉加水分解物がDE約20〜30のものである
前記第2項の基材。 4 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〜第3項いずれか1つの基材。 5 澱粉加水分解物に対して0.1〜10重量%の高
分子物質を含有する前記第1項〜第5項いずれか
1つの基材。
[Scope of Claims] 1 Starch hydrolyzate, seaweed extract, vegetable seed mucilage, vegetable fruit mucilage, vegetable resin-like mucilage, microorganism-produced mucilage, water-soluble or water-dispersible protein, cellulose 1. A base material for powdering a liquid substance, comprising a drum dryer-dried powder of an aqueous dispersion of one or more polymeric substances selected from the group consisting of derivatives and water-soluble synthetic polymers. 2. The base material according to item 1 above, wherein the starch hydrolyzate has a DE (text loin equivalent) of about 30 or less. 3. The base material according to item 2 above, wherein the starch hydrolyzate has a DE of about 20 to 30. 4. The base material according to any one of Items 1 to 3 above, wherein the polymeric substance is a water-soluble or water-dispersible protein. 5. The base material according to any one of Items 1 to 5 above, which contains 0.1 to 10% by weight of a polymeric substance based on the starch hydrolyzate.
JP57187989A 1982-10-25 1982-10-25 Base material for converting liquid material into powder Granted JPS5976538A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57187989A JPS5976538A (en) 1982-10-25 1982-10-25 Base material for converting liquid material into powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57187989A JPS5976538A (en) 1982-10-25 1982-10-25 Base material for converting liquid material into powder

Publications (2)

Publication Number Publication Date
JPS5976538A JPS5976538A (en) 1984-05-01
JPS6152740B2 true JPS6152740B2 (en) 1986-11-14

Family

ID=16215668

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57187989A Granted JPS5976538A (en) 1982-10-25 1982-10-25 Base material for converting liquid material into powder

Country Status (1)

Country Link
JP (1) JPS5976538A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006101823A (en) * 2004-10-08 2006-04-20 Riken Shokuhin Kk Method for evaporating liquid or slurried food to dryness

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5021390A (en) * 1986-09-12 1991-06-04 Hatton John H Liquid hydrocarbon absorbent composition and method
US5059577A (en) * 1986-09-12 1991-10-22 Hatton John H Fluid absorbent composition
US5067984A (en) * 1989-12-19 1991-11-26 Starr Tina F Oil absorbent
US5194280A (en) * 1991-07-15 1993-03-16 F & Mp Research & Development Laboratories, Inc. Method of manufacturing a juice concentrate
JPH0633087A (en) * 1992-07-17 1994-02-08 Nippon Oil & Fats Co Ltd Powdery fat and oil composition
EP3473116A4 (en) * 2016-07-04 2020-02-26 Japan Tobacco Inc. Adsorbent, filter for smoking product which is provided with said adsorbent, and smoking product provided with said filter for smoking products

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006101823A (en) * 2004-10-08 2006-04-20 Riken Shokuhin Kk Method for evaporating liquid or slurried food to dryness

Also Published As

Publication number Publication date
JPS5976538A (en) 1984-05-01

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