JPS623752A - Highly oil absorbing porous powder produced from starch or grain flour as raw material - Google Patents

Highly oil absorbing porous powder produced from starch or grain flour as raw material

Info

Publication number
JPS623752A
JPS623752A JP60141860A JP14186085A JPS623752A JP S623752 A JPS623752 A JP S623752A JP 60141860 A JP60141860 A JP 60141860A JP 14186085 A JP14186085 A JP 14186085A JP S623752 A JPS623752 A JP S623752A
Authority
JP
Japan
Prior art keywords
starch
powder
oil
weight
absorbing porous
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.)
Granted
Application number
JP60141860A
Other languages
Japanese (ja)
Other versions
JPH0697962B2 (en
Inventor
Akira Yamashita
山下 公
Tomoji Sato
友治 佐藤
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.)
Kao Corp
Original Assignee
Kao 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 Kao Corp filed Critical Kao Corp
Priority to JP60141860A priority Critical patent/JPH0697962B2/en
Publication of JPS623752A publication Critical patent/JPS623752A/en
Publication of JPH0697962B2 publication Critical patent/JPH0697962B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Cereal-Derived Products (AREA)
  • Grain Derivatives (AREA)
  • Edible Oils And Fats (AREA)

Abstract

PURPOSE:The titled powder, consisting of starch having a high pregelatination degree and specific surface area and pore diameter satisfying specific conditions, capable of readily powdering a liquid or semisolid fat or oil simply by mixing, having high oil absorption ability and suitable for food, cosmetic, etc. CONSTITUTION:Highly oil absorbing porous powder, obtained by heating starch or grain flour containing >=70wt% starch as a raw material, e.g. with water at >=70 deg.C, to pregelatinize the starch, quickly freezing the resultant pregelatinized material, vacuum freeze-drying the frozen material, pulverizing the freeze-dried material and sieving the resultant powder and having >=80% pregelatinization degree of the starch therein, 1-15mum major axis of powder pores and 3-15m<2>/g specific surface area.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は澱粉又は穀粉を原料とする高吸油能を有する多
孔質粉体に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a porous powder made from starch or grain flour and having high oil absorption ability.

従来から、液体又は半固体の油脂類が食品、化粧品、医
薬品など極めて広い範囲で大量に使用されている。しか
し、液体や半固体は取り扱い上不便であること、また、
種々の製品形態の多様化した粉末製品が要望されるよう
になったことから、液体や半固体の油脂類の粉末化技術
が必要になってきた。
BACKGROUND ART Liquid or semi-solid oils and fats have been used in large quantities in an extremely wide range of fields such as foods, cosmetics, and pharmaceuticals. However, liquids and semi-solids are difficult to handle, and
As demand for diversified powder products in various product forms has increased, technology for powdering liquid and semi-solid oils and fats has become necessary.

〔従来の技術及び問題点〕[Conventional technology and problems]

液体又は半固体の油脂の粉末化法についてはすでにいく
つかの技術が開発されている。例えば、ゼラチンなどを
用いて油脂をカプセル化する方法、又、糖類、デキスト
リン、蛋白質、乳化剤などと共に油脂を乳化後、噴霧乾
燥する方法がよ(知られている。しかし、これらの方法
は高価な装置が必要な上、少量多品種の油脂を粉末化す
るには不適当である。
Several techniques have already been developed for powdering liquid or semi-solid fats and oils. For example, methods of encapsulating fats and oils using gelatin, etc., and methods of emulsifying fats and oils with sugars, dextrins, proteins, emulsifiers, etc. and then spray drying are well known.However, these methods are expensive and expensive. In addition to requiring equipment, it is not suitable for powdering small quantities of a wide variety of oils and fats.

一方、澱粉を主成分とし、これを適切な装置と適度な条
件でα化、乾燥、粉砕することにより、吸油性粉体を製
造する方法が知られている。
On the other hand, a method is known in which oil-absorbing powder is produced by using starch as a main component and gelatinizing, drying, and pulverizing the starch using appropriate equipment and appropriate conditions.

エクストルーダーやドラムドライヤーが代表的装置であ
る。しかし、このような方法によって得られる澱粉は薄
片状であり澱粉1g当たり液体油を2ml程度しか吸収
させることができないのが現状である。又、発泡剤を使
用したほとんどα化していない多孔質澱粉の製造法が知
られており、該多孔質澱粉は吸油性が比較的大きいが、
α化が不十分なため食品においては食感が悪くなるし、
化粧品などではつぶつぶ感が残るなどの問題点がある。
Extruders and drum dryers are typical devices. However, the starch obtained by such a method is flaky and currently only about 2 ml of liquid oil can be absorbed per 1 g of starch. In addition, a method for producing porous starch with almost no gelatinization using a blowing agent is known, and the porous starch has relatively high oil absorption, but
Insufficient gelatinization results in poor texture in foods.
In cosmetics, etc., there are problems such as a lumpy feeling remaining.

以上の現状に鑑み、本発明者らは次の点に注目し研究を
行った。
In view of the above-mentioned current situation, the present inventors conducted research focusing on the following points.

(1)高価な装置を必要とせず、混合するだけで極めて
簡便に液体又は半固体状の油脂を粉末化できること。
(1) Liquid or semi-solid fats and oils can be powdered very simply by simply mixing without the need for expensive equipment.

(2)吸油能が非常に高いこと(Igの澱粉が少なくと
も3m1以上の液体油を吸油し、なおかつ粉体であるこ
と)。
(2) Very high oil absorption capacity (Ig starch absorbs at least 3 ml of liquid oil and is in powder form).

(3)澱粉又は澱粉を70重重量以上含有する穀粉を原
料とし、且つ得られた粉体は常温の水で膨潤、水和する
こと。
(3) Starch or grain flour containing 70 weight or more of starch is used as a raw material, and the resulting powder is swollen and hydrated with water at room temperature.

これら(1)〜(3)の条件を満たすことにより、簡便
に液体又は半固体状油脂を粉末化でき、かつ食品や化粧
品に用いても問題がない高吸油性能を有する粉体を得る
ことが可能になる。
By satisfying these conditions (1) to (3), it is possible to easily powderize liquid or semi-solid fats and oils, and to obtain a powder with high oil absorption performance that can be used in foods and cosmetics. It becomes possible.

〔問題点を解決するための手段〕 本発明者らは研究の結果、澱粉又は澱粉を70重量%以
上含有する穀粉が、その澱粉質のα化度が80%以上で
あり、ある特定条件の多孔質粉体になるとき、上記三条
性を満たすことを見出し本発明を完成する9こ至った。
[Means for solving the problem] As a result of research, the present inventors found that starch or flour containing 70% by weight or more of starch has a degree of gelatinization of starch of 80% or more, and under certain specific conditions. It was discovered that the above-mentioned three-row property is satisfied when the powder is made into a porous powder, leading to the completion of the present invention.

即ち、本発明は、粉体中の澱粉のα化度が80%以上で
あり、粉体の孔径が1〜15μmであり、且つ、比表面
積が3〜15m/gであることを特徴とする、澱粉又は
澱粉を70重量%以上含有する穀粉を原料とする高吸油
性多孔質粉体に係わるものである。
That is, the present invention is characterized in that the degree of gelatinization of starch in the powder is 80% or more, the pore diameter of the powder is 1 to 15 μm, and the specific surface area is 3 to 15 m/g. , relates to a highly oil-absorbing porous powder made from starch or grain flour containing 70% by weight or more of starch.

本発明における?孔質粉体は、その孔径すなわち孔の直
径が1〜15−の範囲内にあることにより高吸油性を示
す。特に3〜10I!rnの孔が総孔数中80%以上あ
ることが望ましい。孔径1−未満では吸油速度が低下す
るし、逆に15−より大きくなると油脂保持力が低下す
ると同時に粉体性が低下する。ただし、製造中に多孔質
粉体の一部が破壊されて15pよりも大きい孔径のもの
が存在したり、1−未満の孔径のものが存在する場合も
あるが、吸油力が低下しない程度に少量ならばその存在
はさしつかえない。本発明では孔径の測定は走査電子顕
微鏡による直接観察法で求めた。
In the present invention? Porous powder exhibits high oil absorption when its pore diameter, that is, the diameter of the pores, is within the range of 1 to 15 −. Especially 3~10I! It is desirable that 80% or more of the total number of holes be rn. If the pore diameter is less than 1-1, the oil absorption rate will decrease, and if the pore diameter is larger than 15-, the oil-holding power will decrease, and at the same time, the powder property will decrease. However, some of the porous powders may be destroyed during production, resulting in the presence of pores larger than 15p, or pores smaller than 1-1, but this may occur to the extent that the oil absorption capacity is not reduced. Its existence is not a problem if it is in small quantities. In the present invention, the pore diameter was determined by direct observation using a scanning electron microscope.

粉体の比表面積は3〜15m/g、好ましくは5〜13
m/gであり、この範囲の比表面積を有するものは高吸
油性を示す。比表面積が3m1g未満では吸油能は2 
ml/g以下となるし、逆に15m/gより大きい場合
は孔径が小さくなり過ぎ、吸油性が低下する。本発明に
おける比表面積値はオーア式比表面積計により窒素ガス
を用いて測定した。
The specific surface area of the powder is 3 to 15 m/g, preferably 5 to 13 m/g.
m/g, and those having a specific surface area within this range exhibit high oil absorption. If the specific surface area is less than 3ml/g, the oil absorption capacity is 2.
ml/g or less, and conversely, if it is larger than 15 m/g, the pore diameter becomes too small and the oil absorption property decreases. The specific surface area value in the present invention was measured using an Ohr type specific surface area meter using nitrogen gas.

本発明における「高吸油性の多孔質粉体」とは、澱粉又
は澱粉を70重量%以上含有する穀粉を原料とし、これ
に種々の加工を加えて、乾燥、粉砕したもので、吸油能
が3 m17g以上のものを指す。本発明でいう「吸油
能」とは、下記の測定法で得られる値である。
In the present invention, "highly oil-absorbing porous powder" refers to starch or flour containing 70% by weight or more of starch as a raw material, which has been subjected to various processing, dried, and ground, and has an oil-absorbing ability. 3. Refers to items of 17g or more. The "oil absorption capacity" as used in the present invention is a value obtained by the following measurement method.

測定法;105℃で1時間乾燥した吸油性多孔質粉体1
gを100 mlのガラスビーカーにとる。次に該吸油
性多孔質粉体にビュ ーレットから菜種油を滴下しながらガ ラス棒で攪拌混合する。粉体が吸油し きれず、滲出した菜種油がビーカー壁 に付着し始めた時点における菜種油滴 下量(ml)を吸油能と定義する。操作は全て20℃で
行う。
Measurement method: Oil-absorbing porous powder 1 dried at 105°C for 1 hour
Take g in a 100 ml glass beaker. Next, rapeseed oil is added dropwise to the oil-absorbing porous powder from a buret while stirring and mixing with a glass rod. The oil absorption capacity is defined as the amount (ml) of rapeseed oil dripped at the time when the powder cannot absorb all the oil and the exuded rapeseed oil starts to adhere to the beaker wall. All operations are performed at 20°C.

通常の生澱粉類、α化澱粉類、穀粉類では吸油能が0.
5 ml/g以下である。一方、本発明による高吸油性
多孔質粉体の吸油能は少なくとも3ml/g以上の値を
示す。
Ordinary raw starches, pregelatinized starches, and grain flours have an oil absorption capacity of 0.
5 ml/g or less. On the other hand, the highly oil-absorbing porous powder according to the present invention exhibits an oil-absorbing capacity of at least 3 ml/g or more.

本発明の原料として用いる澱粉は食用に供されるすべて
の澱粉であり、具体例を挙げれば、トウモロコシ澱粉、
ジャガイモ澱粉、サツマイモ澱粉、米澱粉、くず澱粉、
サゴ澱粉、タピオカ澱粉などである。又、これらを酵素
や酸で加水分解したデキストリンを用いてもよいが、加
水分鮮度が高くなるに従い吸油量が低下するのでDEI
O以下のものが望ましい。
The starch used as a raw material in the present invention includes all edible starches, and specific examples include corn starch, corn starch,
Potato starch, sweet potato starch, rice starch, waste starch,
These include sago starch and tapioca starch. Dextrins hydrolyzed with enzymes or acids may also be used, but as the freshness of the hydrolyzed water increases, the oil absorption decreases, so DEI
O or less is desirable.

又、澱粉を70重量%以上含有する穀粉類も使用に適し
ている。その例としては小麦粉、大麦粉、米粉、ソバ粉
、トウモロコシ粉などのほか、ジャガイモ粉、サツマイ
モ粉などが挙げられる。
Also suitable for use are flours containing 70% by weight or more of starch. Examples include wheat flour, barley flour, rice flour, buckwheat flour, corn flour, as well as potato flour and sweet potato flour.

以上の澱粉又は澱粉を70重量%以上含有する穀粉は、
それぞれ単独で用いても良く、また2種以上混合して使
用しても良い。又、吸油能が低下しない範囲で蛋白質、
糖類、多糖類など澱粉以外の食用成分を併用できるが、
少なくとも澱粉を70重量%以上含むことが必要である
The above starch or flour containing 70% by weight or more of starch is
Each may be used alone or in combination of two or more. In addition, protein, as long as the oil absorption capacity is not reduced.
Edible ingredients other than starch such as sugars and polysaccharides can be used in combination, but
It is necessary to contain at least 70% by weight of starch.

澱粉又は澱粉を70重量%以上含む穀粉から高吸油性多
孔質粉体を製造する好適な方法は次の通りである。
A preferred method for producing highly oil-absorbing porous powder from starch or flour containing 70% by weight or more of starch is as follows.

まず、澱粉又は澱粉を70重世知以上含む穀粉に水又は
温水を加え70℃以上に加熱し、澱粉をα化させる。こ
の時、澱粉のα化度は少なくとも80%以上あることが
必要である。80%未満では十分な吸油量が得られない
上に、食品などに利用した場合ざらつき惑が残ることが
あり好ましくない。又、澱粉又は澱粉を70重世知以上
含む穀粉に対する水又は温水量の比は前者5〜20重量
部に対して後者95〜80重量部が好ましい。
First, water or warm water is added to starch or flour containing 70 times more starch or more and heated to 70° C. or higher to gelatinize the starch. At this time, the degree of gelatinization of starch must be at least 80%. If it is less than 80%, a sufficient amount of oil absorption cannot be obtained, and when used in foods, etc., a rough texture may remain, which is not preferable. The ratio of water or warm water to starch or flour containing 70 parts by weight or more of starch is preferably 5 to 20 parts by weight of the former and 95 to 80 parts by weight of the latter.

水又は温水量がこの比率より大き過ぎても、小さ過ぎて
も吸油量は低下する。
If the amount of water or hot water is too large or too small than this ratio, the oil absorption will decrease.

次にこうして得た澱粉又は澱粉を70重世知以上含む穀
粉のα化物を急速に凍結する。凍結は一30℃以下の温
度で10分以内に急速完全凍結することが望ましい。又
、この凍結工程では凍結速度を大きくするためにα化物
を薄くのばすか、細い線状にすることが望ましい。凍結
方法としては、■液体窒素、液体空気などの極低温ガス
を噴霧又はこれに浸漬する方法、■ブラインに浸漬する
方法、■冷却金属板、ガラス板などに接触させる方法、
■冷却空気による方法、■冷却エタノールに浸漬する方
法等があり、これら■〜■の方法を全て使用することが
できる。
Next, the starch thus obtained or the gelatinized grain flour containing 70 times or more of starch is rapidly frozen. For freezing, it is desirable to quickly and completely freeze within 10 minutes at a temperature of -30°C or less. In addition, in this freezing process, it is desirable to spread the gelatinized product thinly or to form it into a thin line in order to increase the freezing rate. Freezing methods include: ■ Spraying or immersing in cryogenic gas such as liquid nitrogen or liquid air, ■ Immersing in brine, ■ Contacting with a cooling metal plate, glass plate, etc.
There are methods such as (2) using cooled air, (2) immersion in cooled ethanol, and all of these methods (1) to (4) can be used.

続いて、完全凍結した澱粉又は澱粉を70重量%以上含
む穀粉のα化物の乾燥を行う。乾燥処理は凍結したα化
物の氷結晶が融解しない条件で行う必要がある。例えば
、凍結真空乾燥法が代表的な方法として挙げられる。そ
の他の方法として、−1℃以下の温度下でエタノール脱
水する方法も有効である。上記の凍結真空乾燥や凍結エ
タノール脱水は澱粉又は澱粉を70重量%以上含む穀粉
の水分含量が15重量%以下になるまで行う。この後、
更に加熱乾燥、真空乾燥等を行い、水分含量を更に低下
させることも可能である。
Subsequently, completely frozen starch or gelatinized grain flour containing 70% by weight or more of starch is dried. The drying process must be performed under conditions that do not melt the ice crystals of the frozen gelatinized product. For example, freeze-vacuum drying is a typical method. As another method, a method of dehydrating with ethanol at a temperature of −1° C. or lower is also effective. The freeze-vacuum drying and freeze-ethanol dehydration described above are carried out until the moisture content of starch or flour containing 70% by weight or more of starch becomes 15% by weight or less. After this,
Furthermore, it is also possible to further reduce the water content by performing heat drying, vacuum drying, etc.

このようにして得た乾燥物は粉砕機により粉砕し、篩分
けを行う。乾燥後の粉体の粒度は特に制限されないが、
20〜100メソシュ程度にすることが望ましい。
The dried product thus obtained is pulverized by a pulverizer and sieved. The particle size of the powder after drying is not particularly limited, but
It is desirable to set it to about 20 to 100 mesosh.

本発明の高吸油性多孔質粉体を製造する方法としては、
上記の方法以外に噴霧乾燥法やパフィングマシンのよう
な爆裂法でも製造可能である。
The method for producing the highly oil-absorbing porous powder of the present invention includes:
In addition to the above-mentioned methods, it can also be produced by a spray drying method or an explosion method such as a puffing machine.

本発明の高吸油性多孔質粉体は、従来のそれに比し油脂
類をより多く吸収、保持することができる。ここで言う
「油脂類」とは、液体又は半固体の油脂類全てが含まれ
る。例えば大豆油、コーン油、綿実油、菜種油、パーム
油、ヤシ油、魚油、牛脂、豚脂、鯨油などが例示される
ほか、これらの油脂の水素添加物、エステル交換物、分
別物なども含まれる。
The highly oil-absorbing porous powder of the present invention can absorb and retain more fats and oils than conventional powders. The term "fats and oils" as used herein includes all liquid or semi-solid fats and oils. Examples include soybean oil, corn oil, cottonseed oil, rapeseed oil, palm oil, coconut oil, fish oil, beef tallow, lard, and whale oil, as well as hydrogenated products, transesterified products, and fractionated products of these oils and fats. .

又、油脂以外の液状又は半固体状のすべての油溶性物質
も同様に吸収することができる。
In addition, all liquid or semi-solid oil-soluble substances other than fats and oils can be similarly absorbed.

「油溶性物質」とは、例えば、油溶性界面活性剤、炭化
水素、有機溶剤などである。油溶性界面活性剤としては
モノ不飽和脂肪酸グリセリンエステル、炭素数8以下の
モノ飽和脂肪酸グリセリンエステル、不飽和脂肪酸ソル
ビタンエステル、ポリオキシエチレン不飽和脂肪酸ソル
ビタンエステル等が挙げられる。炭化水素としては、流
動パラフィン、リモネン等が、有機溶剤としてはプロピ
レングリコール、エタノール、メタノール等が挙げられ
る。又、油溶性フレーバー等にも適用できる。
"Oil-soluble substances" include, for example, oil-soluble surfactants, hydrocarbons, and organic solvents. Examples of the oil-soluble surfactant include monounsaturated fatty acid glycerin ester, monosaturated fatty acid glycerin ester having 8 or less carbon atoms, unsaturated fatty acid sorbitan ester, polyoxyethylene unsaturated fatty acid sorbitan ester, and the like. Examples of hydrocarbons include liquid paraffin and limonene, and examples of organic solvents include propylene glycol, ethanol, methanol and the like. It can also be applied to oil-soluble flavors and the like.

〔実施例〕〔Example〕

実施例1 トウモロコシ澱粉10重量部に対し、水を90重量部加
え、加熱攪拌しながらα化度が90%の澱粉α化物を製
造した。これをドライアイスーア七トン(約−70℃)
で10分間急速完全凍結し、次に真空凍結乾燥した。次
いで〜粉砕機を用い・真空乾燥物を粉砕後、篩分けして
30メツシュ通過の高吸油性多孔質粉体を得た。
Example 1 90 parts by weight of water was added to 10 parts by weight of corn starch, and a gelatinized starch having a degree of gelatinization of 90% was produced while stirring with heating. Add this to seven tons of dry ice (approximately -70℃)
The mixture was quickly and completely frozen for 10 minutes, and then freeze-dried in a vacuum. Next, the vacuum dried product was pulverized using a pulverizer, and then sieved to obtain a highly oil-absorbing porous powder that passed through 30 meshes.

実施例2 トウモロコシ澱粉10重量部に対し、水を90重量部加
え、加熱攪拌しながらα化度が100%の澱粉α化物を
製造した。これをドライアイス−アセトン(約−70℃
)で急速凍結し、次に真空凍結乾燥した。次いで、粉砕
機を用い、真空乾燥物を粉砕後、篩分けして30メツシ
ュ通過の高吸油性多孔質粉体を得た。
Example 2 90 parts by weight of water was added to 10 parts by weight of corn starch, and a starch gelatinized product having a degree of gelatinization of 100% was produced while stirring with heating. Add this to dry ice-acetone (approximately -70°C).
) and then vacuum freeze-dried. Next, the vacuum dried product was pulverized using a pulverizer, and then sieved to obtain a highly oil-absorbing porous powder that passed through 30 meshes.

実施例3 澱粉含量75%の薄刃小麦粉2重量部に対し、水を98
重量部加え、加熱攪拌しながらα化度が98%の小麦粉
α化物を得た。これを液体窒素で急速凍結した後、真空
凍結乾燥を行った。次に、これを粉砕機を用い粉砕し、
篩分けして20メソシュ通過の高吸油性多孔質粉体を得
た。
Example 3 98% water was added to 2 parts by weight of thin wheat flour with a starch content of 75%.
Parts by weight were added, and while heating and stirring, a gelatinized wheat flour with a degree of gelatinization of 98% was obtained. This was quickly frozen with liquid nitrogen and then vacuum freeze-dried. Next, crush this using a crusher,
The powder was sieved to obtain a highly oil-absorbing porous powder that passed through 20 meshes.

実施例4 ジャガイモ澱粉5重量部に対し、水を95重量部加え、
加熱攪拌しながらα化度85%のジャガイモ澱粉α化物
を得た。この澱粉α化物100gをあらかじめドライア
イスで一70℃まで冷却したエタノール1kgに浸漬し
、10分間急速凍結した。急速凍結後、温度を一5℃ま
で上げ、1時間撹拌し、脱水した。次いでアルコールを
濾過して除き、更に真空下でエタノールを完全に除去し
た。最後に粉砕機を用い粉砕し、篩分けして20メツシ
ュ通過の高吸油性多孔質粉体を得た。
Example 4 95 parts by weight of water was added to 5 parts by weight of potato starch,
While heating and stirring, a gelatinized potato starch with a degree of gelatinization of 85% was obtained. 100 g of this starch gelatinized product was immersed in 1 kg of ethanol that had been previously cooled to -70° C. with dry ice, and rapidly frozen for 10 minutes. After rapid freezing, the temperature was raised to -5°C, stirred for 1 hour, and dehydrated. The alcohol was then filtered off and the ethanol was completely removed under vacuum. Finally, it was crushed using a crusher and sieved to obtain a highly oil-absorbing porous powder that passed through 20 meshes.

実施例5 ジャガイモ澱粉5重量部に対し、水を95重量部加え、
加熱攪拌しながら一α化度100%のジャガイモ澱粉α
化物を得た。この澱粉α化物100gをあらかじめドラ
イアイスで一70°Cまで冷却したエタノール1kgに
浸漬し、10分間急速凍結した。急速凍結後、温度を一
5℃まで上昇させ、1時間攪拌し、脱水した。次いでア
ルコールを濾過して除き、更に真空下でエタノールを完
全に除去した。最後に粉砕機を用い粉砕し、篩分けして
20メツシュ通過の高吸油性多孔質粉体を得た。
Example 5 95 parts by weight of water was added to 5 parts by weight of potato starch,
Potato starch α with a degree of mono-gelatinization of 100% while heating and stirring
I got a monster. 100 g of this starch gelatinized product was immersed in 1 kg of ethanol that had been previously cooled to -70°C with dry ice, and rapidly frozen for 10 minutes. After rapid freezing, the temperature was raised to -5°C, stirred for 1 hour, and dehydrated. The alcohol was then filtered off and the ethanol was completely removed under vacuum. Finally, it was crushed using a crusher and sieved to obtain a highly oil-absorbing porous powder that passed through 20 meshes.

比較例1 トウモロコシ澱粉10重量部に対し、水を90重量部加
え、加熱攪拌しながらα化度が100%の澱粉α化物を
製造した。これを−20℃フリーザーで30分間緩慢凍
結した後、実施例1と同一の方法で真空凍結乾燥、粉砕
、篩分けして30メソシュ通過の粉体を得た。
Comparative Example 1 90 parts by weight of water was added to 10 parts by weight of corn starch, and a gelatinized starch having a degree of gelatinization of 100% was produced while stirring with heating. This was slowly frozen in a -20°C freezer for 30 minutes, and then vacuum freeze-dried, pulverized, and sieved in the same manner as in Example 1 to obtain a powder passing 30 meshes.

比較例2 トウモロコシ澱粉10重量部に対し、水を90重量部加
え、加熱攪拌しながらα化度が30%の澱粉α化物を製
造した。次に、実施例1と同一の方法で急速凍結、真空
凍結乾燥、粉砕、篩分けして30メツシュ通過の粉体を
得た。
Comparative Example 2 90 parts by weight of water was added to 10 parts by weight of corn starch, and a starch gelatinized product having a degree of gelatinization of 30% was produced while stirring with heating. Next, the mixture was rapidly frozen, vacuum freeze-dried, crushed, and sieved in the same manner as in Example 1 to obtain a powder that passed through 30 meshes.

この粉体は、電子顕微鏡による観察では粉末表面の一部
にしか孔が認められず(10〜20声)、比表面積が著
しく小さかった。
When this powder was observed using an electron microscope, pores were observed only in a portion of the powder surface (10 to 20 pores), and the specific surface area was extremely small.

比較例3 トウモロコシ澱粉10重量部に対し、水を90重量部加
え、加熱攪拌しながらα化度が100%の澱粉α化物を
製造した。これを液体窒素中で急速凍結した。次にこれ
を真空凍結乾燥した後、粉砕機を用いて粉砕し、篩分け
して30メツシュ通過の粉体を得た。
Comparative Example 3 90 parts by weight of water was added to 10 parts by weight of corn starch, and a gelatinized starch having a degree of gelatinization of 100% was produced while stirring with heating. This was quickly frozen in liquid nitrogen. Next, this was freeze-dried in vacuum, then ground using a grinder and sieved to obtain a powder that passed through 30 meshes.

比較例4 澱粉含量75%の薄刃小麦粉1重量部に対し、水を99
重量部加え、加熱攪拌しながらα化度が98%の小麦粉
α化物を得た。これを液体窒素中で急速凍結した後、真
空凍結乾燥を行った。次にこれを粉砕機を用いて粉砕し
、篩分けして20メツシュ通過の粉体を得た。
Comparative Example 4 99% of water was added to 1 part by weight of thin blade wheat flour with a starch content of 75%.
Parts by weight were added, and while heating and stirring, a gelatinized wheat flour with a degree of gelatinization of 98% was obtained. This was quickly frozen in liquid nitrogen and then vacuum freeze-dried. Next, this was pulverized using a pulverizer and sieved to obtain a powder that passed through 20 meshes.

試験例1 実施例1〜5及び比較例1〜4で製造した粉体について
吸油能、α化度、孔径、比表面積及び水溶性を測定した
。測定結果は第1表に示した。又、測定法は次に示す方
法を用いた。
Test Example 1 The oil absorption capacity, degree of gelatinization, pore diameter, specific surface area, and water solubility of the powders produced in Examples 1 to 5 and Comparative Examples 1 to 4 were measured. The measurement results are shown in Table 1. In addition, the following measurement method was used.

〈吸油能の測定〉 粉体1gを10On+1ガラスビーカーにとり、菜種油
をビューレットで滴下しながら攪拌混合した。吸油しき
れずに分離した油脂がビーカー壁に付着し始めた時点に
おける菜種油滴下量(ml)を吸油能とした。
<Measurement of oil absorption capacity> 1 g of powder was placed in a 10 On+1 glass beaker, and rapeseed oil was added dropwise using a buret while stirring and mixing. The amount (ml) of rapeseed oil dropped at the time when the separated fats and oils that could not be completely absorbed began to adhere to the beaker wall was defined as the oil absorption capacity.

〈α化度の測定〉 グルコアミラーゼ法を用いた。<Measurement of degree of gelatinization> The glucoamylase method was used.

〈孔径測定〉 走査型電子顕微鏡(日本電子JSM−840)を用い、
金蒸着した後、観察し、孔の直径を測定した。
<Pore size measurement> Using a scanning electron microscope (JEOL JSM-840),
After gold deposition, it was observed and the diameter of the pores was measured.

く比表面積測定〉 島津製作所製オーア式比表面積計21000型により、
窒素ガスを用いて測定した。
Specific surface area measurement〉 Using Ohr type specific surface area meter 21000 manufactured by Shimadzu Corporation,
Measured using nitrogen gas.

く水溶性〉 粉体1gを100 mlの水に加え、攪拌後、水不溶の
白色粒子が残る量を肉眼観察して判定した。
Water Solubility> 1 g of the powder was added to 100 ml of water, and after stirring, the amount of water-insoluble white particles remaining was determined by visual observation.

第  1  表 注)孝1:◎;完全に溶解する。Table 1 Note) Takashi 1: ◎; Completely dissolved.

○;一部不溶物が残る。○: Some insoluble matter remains.

×;はとんど不溶。×: Almost insoluble.

〔発明の効果〕〔Effect of the invention〕

本発明の高吸油性多孔質粉体は、吸油性が優れ、食品、
医薬品、化粧品等で使われる液体又は半固体状を有する
油脂類は勿論のこと、炭化水素類、油溶性界面活性剤な
どをも多量に吸収することができる特性を有する。
The highly oil-absorbing porous powder of the present invention has excellent oil-absorbing properties and can be used in foods,
It has the property of being able to absorb large amounts of liquid or semi-solid oils and fats used in pharmaceuticals, cosmetics, etc., as well as hydrocarbons, oil-soluble surfactants, etc.

従って、本発明品を用いれば、従来取り扱いが不便とさ
れていた油溶性の液状又は半固体状物(油脂など)を、
簡便に粉末化することが可能になる。
Therefore, if the product of the present invention is used, oil-soluble liquid or semi-solid substances (oils and fats, etc.), which were conventionally considered inconvenient to handle, can be
It becomes possible to easily powderize it.

Claims (1)

【特許請求の範囲】[Claims] 1、粉体中の澱粉のα化度が80%以上であり、粉体の
孔径が1〜15μmであり、且つ、比表面積が3〜15
m^2/gであることを特徴とする、澱粉又は澱粉を7
0重量%以上含有する穀粉を原料とする高吸油性多孔質
粉体。
1. The degree of gelatinization of starch in the powder is 80% or more, the pore diameter of the powder is 1 to 15 μm, and the specific surface area is 3 to 15
7 starch or starch, characterized in that m^2/g
A highly oil-absorbing porous powder made from grain flour containing 0% by weight or more.
JP60141860A 1985-06-28 1985-06-28 Method for producing highly oil-absorbing porous powder Expired - Fee Related JPH0697962B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60141860A JPH0697962B2 (en) 1985-06-28 1985-06-28 Method for producing highly oil-absorbing porous powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60141860A JPH0697962B2 (en) 1985-06-28 1985-06-28 Method for producing highly oil-absorbing porous powder

Publications (2)

Publication Number Publication Date
JPS623752A true JPS623752A (en) 1987-01-09
JPH0697962B2 JPH0697962B2 (en) 1994-12-07

Family

ID=15301847

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60141860A Expired - Fee Related JPH0697962B2 (en) 1985-06-28 1985-06-28 Method for producing highly oil-absorbing porous powder

Country Status (1)

Country Link
JP (1) JPH0697962B2 (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004208531A (en) * 2002-12-27 2004-07-29 Kentucky Fried Chicken Japan Ltd Coating material for non-fried food product and method for producing non-fried food product using the same
JP2005237329A (en) 2004-02-27 2005-09-08 Yokohama Kokusai Bio Kenkyusho:Kk Fat solution and / or solid solution of saccharide-fat soluble material, method for producing the same
JP2009504867A (en) * 2005-08-17 2009-02-05 ヴァルティオン テクニリネン ツッツキムスケスクス Compositions of starch-based fillers and coating pigments for fibrous webs and methods for making the same
JP2011514919A (en) * 2008-02-22 2011-05-12 カーギル インコーポレイテッド Pregelatinized starch as a carrier material for liquid components
JP2014212731A (en) * 2013-04-25 2014-11-17 上野製薬株式会社 Powdery oil
JP2014236687A (en) * 2013-06-07 2014-12-18 茂雄 斎藤 Powder-type perilla oil
JP2018082656A (en) * 2016-11-24 2018-05-31 池田食研株式会社 Manufacturing method of oil-soluble substance impregnation foods
US10098833B1 (en) * 2014-11-24 2018-10-16 Amelia Vaughn Formulation and method of use
WO2021084663A1 (en) * 2019-10-30 2021-05-06 株式会社日清製粉グループ本社 Production method for pregelatinized grain flour
JP2021519586A (en) * 2018-03-29 2021-08-12 ストラウス グループ リミテッド Freeze-dried foods and their manufacturing process
EP4056204A4 (en) * 2021-01-05 2023-07-05 Honest Medical China Co., Ltd. Starch-based fluffy particles and preparation method therefor and application thereof
WO2024029516A1 (en) * 2022-08-01 2024-02-08 東和薬品株式会社 Porous carrier particles, functional component-carried particles, and method for producing porous carrier particles

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5755385A (en) * 1980-09-20 1982-04-02 Hitachi Ltd Heat exchanger for cloth dryer with dehumidifying function

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5755385A (en) * 1980-09-20 1982-04-02 Hitachi Ltd Heat exchanger for cloth dryer with dehumidifying function

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004208531A (en) * 2002-12-27 2004-07-29 Kentucky Fried Chicken Japan Ltd Coating material for non-fried food product and method for producing non-fried food product using the same
JP2005237329A (en) 2004-02-27 2005-09-08 Yokohama Kokusai Bio Kenkyusho:Kk Fat solution and / or solid solution of saccharide-fat soluble material, method for producing the same
JP2009504867A (en) * 2005-08-17 2009-02-05 ヴァルティオン テクニリネン ツッツキムスケスクス Compositions of starch-based fillers and coating pigments for fibrous webs and methods for making the same
JP2011514919A (en) * 2008-02-22 2011-05-12 カーギル インコーポレイテッド Pregelatinized starch as a carrier material for liquid components
JP2014212731A (en) * 2013-04-25 2014-11-17 上野製薬株式会社 Powdery oil
JP2014236687A (en) * 2013-06-07 2014-12-18 茂雄 斎藤 Powder-type perilla oil
US10098833B1 (en) * 2014-11-24 2018-10-16 Amelia Vaughn Formulation and method of use
JP2018082656A (en) * 2016-11-24 2018-05-31 池田食研株式会社 Manufacturing method of oil-soluble substance impregnation foods
JP2021519586A (en) * 2018-03-29 2021-08-12 ストラウス グループ リミテッド Freeze-dried foods and their manufacturing process
EP3772995A4 (en) * 2018-03-29 2021-12-29 Strauss Group Ltd. Freeze-dried food products and process of preparing same
WO2021084663A1 (en) * 2019-10-30 2021-05-06 株式会社日清製粉グループ本社 Production method for pregelatinized grain flour
EP4056204A4 (en) * 2021-01-05 2023-07-05 Honest Medical China Co., Ltd. Starch-based fluffy particles and preparation method therefor and application thereof
WO2024029516A1 (en) * 2022-08-01 2024-02-08 東和薬品株式会社 Porous carrier particles, functional component-carried particles, and method for producing porous carrier particles

Also Published As

Publication number Publication date
JPH0697962B2 (en) 1994-12-07

Similar Documents

Publication Publication Date Title
US5624612A (en) Nonaggregating hydrocolloid microparticulates, intermediates therefor, and processes for their preparation
JP3738396B2 (en) Inseparable starch-oil composition
JPS623752A (en) Highly oil absorbing porous powder produced from starch or grain flour as raw material
US5882713A (en) Non-separable compositions of starch and water-immiscible organic materials
KR920007007B1 (en) Low calorie fat substitute
RU2202256C2 (en) Dispersed binder with two-layer coating
Ge et al. Effects of twin-screw extrusion on physicochemical properties and functional properties of bamboo shoots dietary fiber
AU751489B2 (en) Method of preparing dry animal feed
JPH07284380A (en) Production of granular oil-containing food
McDonough et al. Structural Characteristics of Steam‐Flaked Sorghum
CN108272661A (en) A kind of preparation method of eucommia ulmoides seed oil microemulsion
CN111565574A (en) Plant protein based structurant
JPH0343052A (en) Gelatinized cereal and its production
US2904435A (en) Preparation of flaked hull product
Adebiyi et al. Tacca starch citrate-a potential pharmaceutical excipient
JPH02155990A (en) Stabilized oil or fat powder and manufacture thereof
Ahmed Green banana processing, products and functional properties
JP2021093920A (en) Method for producing oil and fat-containing wheat bran powder
JP3501595B2 (en) Production method of powdered fats and oils
JP3808202B2 (en) Powdered food and its manufacturing method
JPH0474361B2 (en)
JPH0216960A (en) Production of dehydrated compressed food
JPS5857217B2 (en) Method for producing fluid granular material containing oil-soluble substance
Azanza et al. Impact of Processing Stages and Additives on the Structural Quality of Cornstarch Bihon-Type Noodles.
JPS60966B2 (en) Manufacturing method for new food materials

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees