JPH0243468B2 - - Google Patents

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Publication number
JPH0243468B2
JPH0243468B2 JP60178557A JP17855785A JPH0243468B2 JP H0243468 B2 JPH0243468 B2 JP H0243468B2 JP 60178557 A JP60178557 A JP 60178557A JP 17855785 A JP17855785 A JP 17855785A JP H0243468 B2 JPH0243468 B2 JP H0243468B2
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Prior art keywords
powder
ethanol
granules
water
hygroscopic
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JPS6240278A (en
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Description

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

〈産業上の利用分野〉 本発明は吸湿性粉末の顆粒製造方法に関する。 〈従来の技術及び発明が解決しようとしている問
題点〉 無定形結晶形の糖類粉末、醗酵乳粉末、粉末コ
ーヒー、粉末果汁、粉末アミノ酸等の吸湿性に富
んだ食用粉末は除湿を施さない場所で加工処理を
行う場合、流動性が悪くまたたく間に固結を生じ
てしまい甚だ取り扱いずらい。一方水又は湯の中
に投入し、溶解させようとしても分散性、崩壊性
が悪い為、所謂ダマとなり溶解しずらく商品価値
を損うものである。 そこで造粒工程を経て該粉末を顆粒化すること
により以降の製造工程中の取り扱いを容易とし、
且、水中に於ける分散性も向上させ、最終製品で
の商品価値を高めようとする努力が為されて来
た。然し蒸気又は水を使用して粉体同志を結着さ
せようとする通常の方法では水分と接触したとこ
ろが急速に部分的にアメ状となり固結し、吸湿性
粉体だけの単品で良好な顆粒を得ることはむずか
しい。その為従来より吸湿性粉末に多量の砂糖の
粉糖とか低D.E.のデキストリンの如き糖類を賦形
剤として加え、蒸気、水等を使用して転動造粒、
押出造粒、流動層造粒等により粉末同志を結着
し、顆粒化する方法がとられているが、この方法
では多量の賦形剤を添加する為、顆粒化しようと
する吸湿性粉末の含有量が少なく吸湿性粉末の単
品のみの顆粒を得ることはとうてい不可能であ
る。 そこで上記湿式造粒法に代り水分を加えること
なく該粉末をシート状に圧縮後破砕して顆粒化す
る乾式造粒方法が挙げられるが、該方法により得
られた顆粒は硬度的に硬い為、水または湯中への
沈降を速くすることは出来るが分散性、溶解性が
甚だ悪く、その為口溶けもよくないという欠点が
ある。 以上の理由により長年に亘りソフトで且分散
性、溶解性に優れた吸湿性粉末の単品で顆粒を得
るべく努力がなされており過去に於て (1) 特公昭54−2259に低温度下において、粉末ア
ミノ酸、粉末醤油、粉末味噌、粉末コーヒー等
の易吸湿性食用微粉末に、低含水率の高純度ア
ルコールを加えて、これを練合した後、常法に
より粒化し、真空乾燥することを特徴とする易
吸湿性食用微粉末の粒化法。 (2) 特公昭47−15722に食塩、糖類、有機酸、粉
末醤油、動植物エキス粉末、タンパク分解物、
化学調味料等の水溶性粉末原料からなる吸湿
性、潮解性を有する粉末食品を造粒するに際
し、エチルアルコール、又はメチルアルコール
等のアルコール類の含有水溶液を原料重量に対
し、害水分が0.1〜5%になる範囲で添加混合
したのち乾燥して結着造粒することを特徴とす
る即溶性顆粒食品の製造法が開示されている。 然しながら(1)の方法によれば易吸湿性食微粉末
にエタノールを加え練合し、団塊状になす為には
当該粉末に対し、凡そ30%近辺以上のエタノール
を加える必要があり、しかるのち添加したエタノ
ールを真空乾燥機を使用して飛散させるのである
が、かかる多量のエタノールを蒸散させるには原
価的にかなりのコスト高となり、危険性もある。
またエタノールを回収して再使用する場合は回収
設備も大掛りとなり経済的でない。 (2)の方法によれば吸湿性、潮解性を有する粉末
食品を造粒するのに際し、有機酸、粉末醤油、動
植物エキス粉末、タンパク分解物、化学調味料に
比べて比較的吸湿性の強くない食塩、糖類を当該
特許公報の実施例1、2に示す如く半分以上含有
せしめて一種の賦形剤的な作用効果をもたせて造
粒している。故に極めて容易に造粒出来るのであ
り、本発明は極めて吸湿性の強い無定形結晶形の
糖類、醗酵乳粉末、コーヒー粉末、粉末醤油、ア
ミノ酸粉末、野菜粉末、果汁粉末等のみをエタノ
ール又は水含有エタノールに添加混合後、加湿空
気に接触させてから乾燥して整粒すると、意外と
該引用公報に比べ分散性、溶解性の優れた顆粒が
得られる。(後述の試験例2参照) 〈問題点を解決するための手段及び作用〉 本発明者等は前述の欠陥を改善すべく鋭意研究
の結果、吸湿性の低脂質粉末にエタノール又は水
含有エタノールを加え、賦形剤を使用することな
く均一に混合したのち加湿空気に接触させ、顆粒
化することを特徴とする吸湿性粉末の顆粒製造方
法を完成するに至つた。 即ち本発明に於ける吸湿性粉末とは無定形結晶
形の糖類粉末、一般に脂肪含有量1.5重量%以下
の低脂質含有脱脂粉乳より調製した醗酵乳粉末、
コーヒー粉末、粉末醤油、アミノ酸粉末、野菜粉
末、果汁粉末等の様な著しく吸湿性の高い粉末を
指称しているが、シヨ糖、ブドウ糖、乳糖の粉
糖、或いはココアの如き比較的吸湿性の弱い粉末
類も顆粒化出来ることは当然である。 またエタノールとは通常入手出来る局方無水エ
タノール、試薬特級エタノール、食添エタノール
等をいい、若干の水分を含有している。吸湿性粉
末に添加するエタノール中の水分量が該吸湿性粉
末に対して2重量%程度以下であり、該量を越え
ると当該粉末は処理工程中にアメ状に固結し、分
散性、溶解性の良い顆粒を得ることが出来ない。
(試験例1参照) 吸湿性粉末にエタノール又は水含有エタノール
を添加し、均一に混合する方法としては粉末中に
エタノール又は水含有エタノールを少量づつ滴下
し、練合する方法、粉末を回転釜、円筒状ドラム
等で転動させながらエタノール又は水含有エタノ
ールをスプレーする方法等が有り、当該添加操作
を粉末の吸湿性を考慮して、低温、低湿度で行う
ことが好ましく例えば絶対湿度0.01〔Kg−水蒸
気/Kg−乾き空気〕程度以下が好ましい。もし低
温でも高湿度の雰囲気中で作業を実施した場合、
エタノール又は水含有エタノールが均一に混合分
散される前に粉末は吸湿してしまいアメ状に固ま
り以降の作業が出来ない。 次に上記の如くエタノール又は水含有エタノー
ルを吸湿性粉末に添加混合する時のエタノールと
しての添加量は該粉末に対して2重量%程度以上
であり、上限には特に規制はないが経済性、危険
性の見地より20重量%程度までである。 斯くの如くしてエタノール又は水含有エタノー
ルと均一に混合された吸湿性粉末の外観はサラサ
ラした取り扱い易い流動性を帯びた粉末となる。 次に上記の如くして得たサラサラとなつた吸湿
性粉末を圧力を加えず加湿雰囲気内を自然落下或
いは自然放置の状態で粒子を多数付着せしめてか
ら乾燥後再度整粒することによつて分散性、溶解
性のよい顆粒を得る。即ちその為には水蒸気を発
生せしめたホイロ、スチームオーブン或は円塔内
に蒸気を吹き込ませ加湿した雰囲気を作り、エタ
ノール又は水含有エタノールを添加混合した粉末
を上記装置内に放置又は落下させることにより加
湿空気とゆるやかに接触させ水分活性値として
0.30〜0.74程度に調整する。かかる操作により粉
末同志は多数点で相互に付着を生じ団塊状とな
る。該団塊状品を通常の熱風乾燥装置によつてエ
タノールと余剰の水分を飛散させ、放冷後篩別工
程を経て整粒する。 実施例 1 コーヒー生豆13.9Kgを直火式コーヒーロースタ
ー(FUJI MFG社製)で200℃、10分間焙焼して
11.4Kgの焙焼豆を得た。この焙焼豆をコーヒーミ
ル(FUJI MFG社製)で粉砕し98℃の熱湯104.6
Kgで抽出し、手持屈折計でBx2゜(以下同様の測定
器)の抽出液85.7Kgを得た。該抽出液を真空濃縮
機(ALFA−LAVAL社製)でBx30゜まで濃縮後
アトマイザー式スプレードライヤーを用いて乾燥
し水分1重量%、水分活性Aw(以下同様)0.25の
コーヒー粉末を得た。該コーヒー粉末1Kgを回転
釜に入れ20℃相対湿度(RH)(以下同様)40%
の雰囲気中で回転させながら含水率5.0重量%の
エタノール70mlをスプレーしながら均一に混合し
た。 温度55℃、RH81%の加湿空気を高さ2メート
ル、直径0.8メートルの円塔内に側壁より吹き込
みながら、該エタノール含有コーヒー粉末を20メ
ツシユ(日本工業規格、以下同様)の篩を通過さ
せながら該円塔内を上方より落下させ、加湿空気
に1秒間接触させた。該円塔より出た団塊状品は
瑞西ロトロニツク社製水分活性測定システムハイ
ドロスコープDT型を用いてAwを測定した(以
下同様)。その結果Aw0.45のコーヒー団塊状品
1059gを得た。該団塊状品を金網のツレーに厚さ
0.5mmに拡げて静置したままで50℃1時間乾燥し
た後10メツシユ篩を通して整粒し、水分2重量%
のコーヒー顆粒970gを得た。 この顆粒を後記、試験例1と同様な方法で15℃
の水道水中の溶解性を調べた結果未顆粒のコーヒ
ー粉末の溶解時間は、10秒であつたのに対し本発
明により得られた顆粒品は5秒であり、未顆粒品
に比べ溶解性が優れていた。未顆粒品と本発明に
より得られた顆粒に関して専門家パネル20人によ
り官能検査を行なつた判定は、未顆粒品と、本発
明により得られた顆粒の味の違いについて行ない
クレーマーの検定法を用い危険率5%で行なわれ
た。 結果は下表に示される通りであり、未顆粒品と
本発明により得られた顆粒の味の差は認められな
かつた。
<Industrial Application Field> The present invention relates to a method for producing granules of hygroscopic powder. <Problems to be solved by the prior art and the invention> Highly hygroscopic edible powders such as amorphous crystalline saccharide powder, fermented milk powder, powdered coffee, powdered fruit juice, powdered amino acids, etc. should be stored in a place that is not dehumidified. When processing, it has poor fluidity and caking occurs quickly, making it extremely difficult to handle. On the other hand, even if it is poured into water or hot water and an attempt is made to dissolve it, the dispersibility and disintegration properties are poor, resulting in so-called lumps that are difficult to dissolve and reduce the commercial value. Therefore, by granulating the powder through a granulation process, it is easier to handle during the subsequent manufacturing process,
Efforts have also been made to improve the dispersibility in water and increase the commercial value of the final product. However, in the conventional method of using steam or water to bind powders together, the parts that come into contact with moisture quickly become candy-like and solidify, making it difficult to form good granules with only hygroscopic powder. is difficult to obtain. Therefore, conventionally, a large amount of sugar such as powdered sugar or low DE dextrin is added to hygroscopic powder as an excipient, and tumble granulation is carried out using steam, water, etc.
Extrusion granulation, fluidized bed granulation, etc. are used to bind powders together and granulate them, but this method adds a large amount of excipients, so the hygroscopic powder to be granulated is It is almost impossible to obtain single granules of hygroscopic powder with a small content. Therefore, instead of the above-mentioned wet granulation method, there is a dry granulation method in which the powder is compressed into a sheet shape and then crushed into granules without adding moisture, but since the granules obtained by this method are hard, Although it can speed up sedimentation in water or hot water, it has extremely poor dispersibility and solubility, and therefore does not dissolve well in the mouth. For the above reasons, efforts have been made for many years to obtain granules from a single hygroscopic powder that is soft and has excellent dispersibility and solubility. , high-purity alcohol with low moisture content is added to easily hygroscopic edible fine powder such as powdered amino acids, powdered soy sauce, powdered miso, powdered coffee, etc., and after kneading this, it is granulated by a conventional method and vacuum-dried. A method for granulating easily hygroscopic edible fine powder characterized by: (2) Special Publication No. 47-15722, salt, sugars, organic acids, powdered soy sauce, animal and plant extract powders, protein decomposition products,
When granulating powder foods with hygroscopic and deliquescent properties made from water-soluble powder raw materials such as chemical seasonings, an aqueous solution containing alcohols such as ethyl alcohol or methyl alcohol is mixed with a harmful water content of 0.1 to 0.1 to A method for producing a ready-to-dissolve granular food is disclosed, which is characterized by adding and mixing ingredients in a range of 5%, followed by drying and binding and granulation. However, according to method (1), it is necessary to add ethanol to the easily hygroscopic edible powder and knead it, and in order to form it into a lump, it is necessary to add approximately 30% or more of ethanol to the powder. The added ethanol is dispersed using a vacuum dryer, but evaporating such a large amount of ethanol is quite costly and dangerous.
Furthermore, if ethanol is to be recovered and reused, the recovery equipment will be large-scale, which is not economical. According to method (2), when granulating a powdered food that has hygroscopicity and deliquescent properties, it has a relatively strong hygroscopicity compared to organic acids, powdered soy sauce, animal and plant extract powders, protein decomposition products, and chemical seasonings. As shown in Examples 1 and 2 of the patent publication, more than half of the salt and saccharides are contained in the granules to provide a type of excipient effect. Therefore, it is extremely easy to granulate, and the present invention uses only highly hygroscopic amorphous crystalline saccharides, fermented milk powder, coffee powder, powdered soy sauce, amino acid powder, vegetable powder, fruit juice powder, etc., into granules containing ethanol or water. After adding and mixing with ethanol, contacting with humid air, drying and sizing, granules with better dispersibility and solubility than those in the cited publication are surprisingly obtained. (See Test Example 2 below) <Means and effects for solving the problem> As a result of intensive research to improve the above-mentioned defects, the present inventors added ethanol or water-containing ethanol to a hygroscopic low-lipid powder. In addition, we have completed a method for producing granules of hygroscopic powder, which is characterized by uniformly mixing without using excipients and then contacting with humidified air to form granules. That is, the hygroscopic powder in the present invention refers to amorphous crystalline saccharide powder, generally fermented milk powder prepared from low-fat skim milk powder with a fat content of 1.5% by weight or less,
It refers to extremely hygroscopic powders such as coffee powder, powdered soy sauce, amino acid powder, vegetable powder, fruit juice powder, etc., but relatively hygroscopic powders such as sucrose, glucose, lactose powdered sugar, or cocoa. It goes without saying that weak powders can also be granulated. Ethanol refers to commonly available pharmacopoeia anhydrous ethanol, reagent grade ethanol, food-added ethanol, etc., and contains some water. The amount of water in the ethanol added to the hygroscopic powder is approximately 2% by weight or less based on the hygroscopic powder. If this amount is exceeded, the powder will solidify into a candy-like shape during the processing process, resulting in poor dispersibility and dissolution. It is not possible to obtain granules with good quality.
(See Test Example 1) Methods for adding ethanol or water-containing ethanol to hygroscopic powder and mixing uniformly include dropping ethanol or water-containing ethanol into the powder little by little and kneading, or mixing the powder in a rotary pot. There is a method of spraying ethanol or water-containing ethanol while rolling it with a cylindrical drum, etc., and it is preferable to perform the addition operation at a low temperature and low humidity, considering the hygroscopicity of the powder, for example, at an absolute humidity of 0.01 [Kg]. - water vapor/Kg - dry air] or less is preferable. If work is carried out in an atmosphere of high humidity even at low temperatures,
Before the ethanol or water-containing ethanol is evenly mixed and dispersed, the powder absorbs moisture and hardens into a candy-like consistency, making subsequent operations impossible. Next, when ethanol or water-containing ethanol is added and mixed into the hygroscopic powder as described above, the amount of ethanol added is about 2% by weight or more based on the powder, and there is no particular upper limit, but it is economical. From the standpoint of danger, it is limited to about 20% by weight. The appearance of the hygroscopic powder uniformly mixed with ethanol or water-containing ethanol in this manner is a smooth and fluid powder that is easy to handle. Next, the smooth hygroscopic powder obtained as described above is allowed to fall naturally in a humidified atmosphere without applying pressure, or left to adhere to a large number of particles, and after drying, the powder is sized again. Obtain granules with good dispersibility and solubility. That is, in order to do this, steam is blown into a foil, steam oven, or circular tower that generates water vapor to create a humidified atmosphere, and ethanol or a powder mixed with water-containing ethanol is left or dropped into the above device. The water activity value is measured by gently contacting humidified air with
Adjust to about 0.30 to 0.74. Through this operation, the powders adhere to each other at multiple points and form a lump. Ethanol and excess moisture are removed from the nodules using a conventional hot air drying device, and after cooling, the nodules are sized through a sieving process. Example 1 13.9 kg of green coffee beans were roasted at 200℃ for 10 minutes in an open flame coffee roaster (manufactured by FUJI MFG).
11.4Kg of roasted beans were obtained. The roasted beans are ground with a coffee mill (manufactured by FUJI MFG) and heated with 98°C boiling water at 104.6°C.
Kg was extracted using a hand-held refractometer to obtain 85.7 Kg of Bx2° extract (hereinafter referred to as the same measuring device). The extract was concentrated to Bx30° using a vacuum concentrator (manufactured by ALFA-LAVAL) and dried using an atomizer spray dryer to obtain coffee powder with a water content of 1% by weight and a water activity Aw (hereinafter the same) of 0.25. Put 1 kg of the coffee powder into a rotary pot and heat at 20°C relative humidity (RH) (hereinafter the same) 40%.
70 ml of ethanol with a moisture content of 5.0% by weight was sprayed on the mixture to mix it uniformly while rotating in an atmosphere of . While blowing humidified air at a temperature of 55°C and RH of 81% from the side wall into a circular tower with a height of 2 meters and a diameter of 0.8 meters, the ethanol-containing coffee powder was passed through a 20 mesh sieve (Japanese Industrial Standards, hereinafter the same). The inside of the circular tower was dropped from above and brought into contact with humidified air for 1 second. The Aw of the nodules discharged from the circular tower was measured using a water activity measuring system Hydroscope DT model manufactured by Zuisai Rotronik Co., Ltd. (the same applies hereinafter). As a result, Aw0.45 coffee baby-like products
Obtained 1059g. Thickness
Spread it to 0.5 mm and leave it to dry at 50℃ for 1 hour, then pass it through a 10-mesh sieve to size the particles, and the moisture content is 2% by weight.
970g of coffee granules were obtained. These granules were prepared at 15°C in the same manner as in Test Example 1 as described below.
As a result of investigating the solubility of coffee powder in tap water, the dissolution time of ungranulated coffee powder was 10 seconds, while the granulated product obtained by the present invention was 5 seconds, indicating that the solubility was lower than that of ungranulated coffee powder. It was excellent. A sensory test was conducted by a panel of 20 experts on the ungranulated product and the granules obtained according to the present invention. The test was carried out with a risk of 5%. The results are shown in the table below, and no difference in taste was observed between the ungranulated product and the granules obtained according to the present invention.

【表】 評価…有意差なし
実施例 2 搾汁温州オレンジ果汁6Kgに対し粉末デキスト
リン(DE30)0.6Kgを加え、よく撹拌混合後、ア
トマイザー式スプレードライヤーにて乾燥してオ
レンジ果汁粉末を得た。該果汁粉末1Kgに25℃
RH50%の室内で含水率0.5重量%のエタノールを
滴下させながら混合機で均一に混合した。混合後
0.2cmの厚さに均一にトレー上に拡げ、27℃RH65
%の加湿空気中に130秒間接触させAw0.50の団塊
状品1050gを得た。該団塊状品を40℃で1時間30
分乾燥し水分2重量%とした後10メツシユの篩を
通して果汁顆粒970gを得た。 得られた顆粒は試験例1と同様な方法により15
℃の水道水中での溶解性を調べた結果オレンジ果
汁粉末は、15秒であつたのに対し、本発明により
得られた顆粒は8秒であり、未顆粒品に比べ溶解
性は優れていた。 未顆粒品と本発明で得られた顆粒の味の差は実
施例1と同様の方法で行ない。その結果は下表に
示される通りであり、未顆粒品と本発明で得られ
た顆粒の味の差は認められなかつた。
[Table] Evaluation: No significant difference Example 2 0.6 kg of powdered dextrin (DE30) was added to 6 kg of squeezed Unshu orange juice, stirred and mixed well, and dried with an atomizer spray dryer to obtain orange juice powder. 1 kg of the fruit juice powder at 25℃
Ethanol with a water content of 0.5% by weight was added dropwise in a room with a RH of 50% and mixed uniformly using a mixer. After mixing
Spread it evenly on a tray to a thickness of 0.2 cm and store at 27℃RH65.
% humidified air for 130 seconds to obtain 1050 g of nodules having an Aw of 0.50. The baby-shaped product was heated at 40℃ for 1 hour.
After drying for several minutes to reduce the moisture content to 2% by weight, the mixture was passed through a 10-mesh sieve to obtain 970 g of fruit juice granules. The obtained granules were processed in the same manner as in Test Example 1.
As a result of examining the solubility in tap water at ℃, it was 15 seconds for orange juice powder, but 8 seconds for the granules obtained by the present invention, which showed that the solubility was superior to that of ungranulated products. . The difference in taste between the ungranulated product and the granules obtained according to the present invention was determined in the same manner as in Example 1. The results are shown in the table below, and no difference in taste was observed between the ungranulated product and the granules obtained according to the present invention.

【表】 評価…有意差なし
実施例 3 乾燥椎茸2Kgに水18Kgを加え80℃に加温後1時
間放置し、バスケツト型遠心分離機にてエキス分
を分別し、真空濃縮機でBx30゜まで濃縮後アトマ
イザー式スプレードライヤーにて乾燥する。得ら
れた200メツシユ以下の椎茸エキス粉末1Kgを25
℃RH50%の室内で二軸式ニーダーに入れ含水率
0.5重量%のエタノール50mlをスプレーしながら
80rpmで3分間均一に混合する。その後厚さ0.3
cmに拡げて25℃RH66%の加湿空気に180秒間接
触させAw0.30の団塊状品を得た。次に50℃で1
時間通風乾燥し、10メツシユの篩を通過させ水分
2.5重量%の顆粒950gを得た。 この顆粒は試験例1と同様な方法により15℃の
水道水中で溶解性を調べた結果、椎茸エキス粉末
は、12秒であつたのに対し本発明により得られた
顆粒は7秒であり未顆粒品に比べ溶解性が優れて
いた。 尚、未顆粒品と本発明により得られた顆粒の味
の差は実施例1と同様な方法で行なつた。その結
果は下表に示される通りであり、未顆粒品と本発
明により得られた顆粒の味の差は認められなかつ
た。
[Table] Evaluation: No significant difference Example 3 Add 18 kg of water to 2 kg of dried shiitake mushrooms, heat to 80°C, leave for 1 hour, separate the extract with a basket centrifuge, and use a vacuum concentrator to reduce Bx30°. After concentration, dry with an atomizer spray dryer. 1 kg of shiitake mushroom extract powder of less than 200 mush is 25
Moisture content in a twin-screw kneader in a room at ℃RH50%
While spraying 50ml of 0.5% ethanol.
Mix evenly for 3 minutes at 80 rpm. Then thickness 0.3
It was spread to a size of 1.5 cm and brought into contact with humidified air at 25°C and RH 66% for 180 seconds to obtain a nodular product with an Aw of 0.30. Then 1 at 50℃
Dry with ventilation for an hour and pass through a 10-mesh sieve to remove moisture.
950 g of 2.5% by weight granules were obtained. The solubility of these granules was examined in tap water at 15°C using the same method as in Test Example 1. The solubility of the shiitake extract powder was 12 seconds, while that of the granules obtained by the present invention was 7 seconds. It had better solubility than granules. The difference in taste between the ungranulated product and the granules obtained according to the present invention was determined in the same manner as in Example 1. The results are shown in the table below, and no difference in taste was observed between the ungranulated product and the granules obtained according to the present invention.

【表】 評価…有意差なし
実施例 4 剥皮した玉葱を熱風乾燥後粉砕したAw0.36の
玉葱粉末1Kgを回転釜に入れ20℃RH40%の雰囲
気中で含水率10重量%のエタノール200mlをスプ
レーしながら均一に混合した。 55℃RH81%の加湿空気が高さ2m、直径0.8m
の円塔内に側壁より吹き込みながら、該エタノー
ル含有玉葱粉末を20メツシユの篩を通過させなが
ら該円塔内を上方より落下させ、加湿空気に1秒
間接触させ団塊状品を1100g得る。該団塊状品の
Awは0.55である。該団塊状品を流動層乾燥機で
70℃10分間乾燥し、10メツシユの篩を通して水分
含有量3重量%の顆粒を得る。 得られた顆粒は試験例1と同様な方法により15
℃の水道水中で溶解性を調べた結果、玉葱粉末の
溶解時間は、15秒であつたのに対し本発明により
得られた顆粒品は8秒であり、本発明により得ら
れた顆粒は溶解性が優れていた。 尚未顆粒品と本発明により得られた顆粒の味の
差は実施例1と同様な方法で行なつた。 その結果は下表に示される通りであり、未顆粒
品と本発明で得られた顆粒の味の差は認められな
かつた。
[Table] Evaluation: No significant difference Example 4 1 kg of onion powder with Aw0.36, which was obtained by drying peeled onions with hot air and pulverizing them, was placed in a rotary pot and sprayed with 200 ml of ethanol with a moisture content of 10% by weight in an atmosphere of 20°C and RH40%. Mix evenly. Humidified air at 55℃RH81% height 2m, diameter 0.8m
The ethanol-containing onion powder was passed through a 20-mesh sieve while being blown from the side wall into the circular tower, and dropped from above into the circular tower, and was brought into contact with humidified air for 1 second to obtain 1100 g of nodules. of the baby-boom-like product
Aw is 0.55. The nodules are dried in a fluidized bed dryer.
Dry at 70°C for 10 minutes and pass through a 10 mesh sieve to obtain granules with a water content of 3% by weight. The obtained granules were processed in the same manner as in Test Example 1.
As a result of examining the solubility in tap water at a temperature of It had excellent characteristics. The difference in taste between the ungranulated product and the granules obtained according to the present invention was determined in the same manner as in Example 1. The results are shown in the table below, and no difference in taste was observed between the ungranulated product and the granules obtained according to the present invention.

【表】 評価…有意差なし
実施例 5 実施例1と同様な方法で得られたコーヒー粉末
1Kgを、20℃RH40%の雰囲気中で回転釜を用
い、含水率5.0重量%のエタノール70mlをスプレ
ー容器を用いスプレーしよく混合した。 得られたエタノール含有コーヒー粉末を40cm×
25cmのツレー上に厚さ0.3cmに敷き詰めて30℃
RH78%の加湿空気に300秒接触させてAw0.55の
コーヒー団塊状品1040gを得た。このものを70℃
で15分間乾燥してエタノールを飛散させ、水分2
重量%まで乾燥したのち10メツシユの篩を通して
篩別してコーヒー顆粒970gを得た。この顆粒を
試験例1と同様な方法で15℃の水道水の中で溶解
性を調べた結果コーヒー粉末は15秒であつたのに
対し本発明により得られた顆粒品は7秒であり未
顆粒品に比べ溶解性は優れていた。 未顆粒品と、本発明により得られた顆粒の味の
差は実施例1と同様な方法で行なつた。 その結果は、下表に示される通りであり、未顆
粒品と、本発明で得られた顆粒の味の差は認めら
れなかつた。
[Table] Evaluation: No significant difference Example 5 1 kg of coffee powder obtained in the same manner as in Example 1 was sprayed with 70 ml of ethanol with a water content of 5.0% by weight using a rotary pot in an atmosphere of 20°C and RH 40%. Spray and mix well using a container. The obtained ethanol-containing coffee powder was placed in a 40cm x
Spread on a 25cm tree to a thickness of 0.3cm and heat at 30℃.
It was brought into contact with humidified air at RH78% for 300 seconds to obtain 1040g of coffee nodules with Aw0.55. This stuff at 70℃
Dry for 15 minutes to scatter the ethanol and remove the moisture.
After drying to % by weight, it was sieved through a 10 mesh sieve to obtain 970 g of coffee granules. The solubility of the granules was examined in tap water at 15°C in the same manner as in Test Example 1. The solubility of the coffee powder was 15 seconds, but the solubility of the granules obtained by the present invention was 7 seconds. The solubility was superior to that of granules. The difference in taste between the ungranulated product and the granules obtained according to the present invention was determined in the same manner as in Example 1. The results are shown in the table below, and no difference in taste was observed between the ungranulated product and the granules obtained according to the present invention.

【表】 評価…有意差なし
実施例 6 1−ケストール、ニストース、1F−フラクト
フラノシルニストース等を主成分とする水分1.5
重量%の無定形結晶形のフラクトオリゴ糖粉末1
Kgを20℃RH40%の室内で混合撹拌しながら含水
率2.5重量%のエタノール20mlを滴下し均一にす
る。該エタノール含有フラクトオリゴ糖粉末を厚
0.15cmに拡げ30℃78%の加湿空気に125秒間接触
させAw0.34の団塊状品を1010g得た。該品を70
℃で15分間乾燥後、10メツシユの篩を通して水分
2重量%のフラクトオリゴ糖顆粒を980g得た。 この顆粒を試験例1と同様な方法で15℃の水道
水中で溶解性を調べた結果フラクトオリゴ糖粉末
は4分55秒であつたに対し本発明によつて得られ
た、顆粒品は2分5秒であり未顆粒品に比べ溶解
性が優れていた。 未顆粒品と本発明により得られた顆粒の味の差
は実施例1と同様な一方法で行なつた。その結果
は下表に示される通りであり、未顆粒品と本発明
で得られた顆粒の味の差は認められなかつた。
[Table] Evaluation: No significant difference Example 6 Moisture mainly composed of 1-kestol, nystose, 1F-fructofuranosylnystose, etc. 1.5
Wt% fructooligosaccharide powder in amorphous crystalline form 1
20 ml of ethanol with a moisture content of 2.5% by weight is added dropwise to the mixture while stirring in a room at 20°C and RH 40%. The ethanol-containing fructooligosaccharide powder is
It was spread to 0.15 cm and brought into contact with humidified air at 30° C. and 78% for 125 seconds to obtain 1010 g of nodules having an Aw of 0.34. 70 for the item
After drying at °C for 15 minutes, the mixture was passed through a 10 mesh sieve to obtain 980 g of fructooligosaccharide granules with a water content of 2% by weight. The solubility of these granules was examined in tap water at 15°C in the same manner as in Test Example 1. As a result, the solubility of the fructooligosaccharide powder was 4 minutes and 55 seconds, whereas that of the granules obtained by the present invention was 2 minutes. The dissolution time was 5 seconds, and the solubility was superior to that of the ungranulated product. The difference in taste between the ungranulated product and the granules obtained according to the present invention was determined by the same method as in Example 1. The results are shown in the table below, and no difference in taste was observed between the ungranulated product and the granules obtained according to the present invention.

【表】 評価…有意差なし
試験例 1 25℃RH50%の室内で実施例4で使用した
Aw0.36の玉葱粉末1Kgに対して含水率10重量%
のエタノールをそれぞれ表−1の如く添加混合し
て均一化する。該混合物を厚さ0.15cmに敷き拡げ
30℃RH98%の加湿雰囲気中120秒放置し団塊状
とした。この時のAwを表−1に示した。該団塊
状品をそれぞれ70℃で15分間通風乾燥し10メツシ
ユの篩を通して水分2.5重量%の顆粒品を得た。
該顆粒品が5、10、15、20℃の各水温に溶解する
までの時間を表−1に示した。溶解する時間とは
100mlビーカーに各水準の水温の水を50mlづつ採
取し、この中に直径5mm、長さ15mmの電磁式撹拌
子を投入し、ヤマト科学(株)製(M−21型)スター
ラー上に設置し、別途秤量した各試料1.0gを上
記ビーカー内に投入と同時にダイヤル0.5で回転
撹拌して試料が完全に溶解するまでの時間(秒)
を測定する。
[Table] Evaluation: No significant difference Test example 1 Used in Example 4 indoors at 25℃RH50%
Moisture content 10% by weight per 1kg of onion powder with Aw0.36
Add and mix ethanol as shown in Table 1 to homogenize. Spread the mixture to a thickness of 0.15 cm.
It was left in a humidified atmosphere at 30°C and RH 98% for 120 seconds to form a nodule. The Aw at this time is shown in Table-1. Each of the nodules was air-dried at 70° C. for 15 minutes and passed through a 10-mesh sieve to obtain granules with a moisture content of 2.5% by weight.
Table 1 shows the time taken for the granules to dissolve at each water temperature of 5, 10, 15, and 20°C. What is the time to dissolve?
50 ml of water at each level of water temperature was collected in a 100 ml beaker, and an electromagnetic stirrer with a diameter of 5 mm and a length of 15 mm was placed in the beaker, and the mixture was placed on a stirrer manufactured by Yamato Scientific Co., Ltd. (Model M-21). , put 1.0g of each sample weighed separately into the above beaker and at the same time stir with a dial of 0.5. Time (seconds) until the sample is completely dissolved.
Measure.

【表】【table】

【表】 表−1に示した如く玉葱粉末に対する添加水分
の量が2重量%を越えると得られた顆粒の水中で
の溶解性が低下する。 試験例 2 実施例6と同様のフラクトオリゴ糖粉末及び水
分3重量%の醗酵乳粉末に対して局方無水エタノ
ールを各々1、2、3、7、10、20重量%づつ添
加し25℃RH50%の作業場内で均一に混合した。
得られた混合物を0.2cm厚に敷き詰めた後温度30
℃、RH100%の雰囲気中に50秒間放置し、Awを
測定した。(表−2参照) 得られた夫々の顆粒を50℃で1時間通風乾燥
し、水分1.5重量のフラクトオリゴ糖団塊状品及
び水分3重量%醗酵乳団塊状品を10メツシユの篩
を通過させて整粒し顆粒化した。 本試験で得られたフラクトオリゴ糖顆粒及び醗
酵乳顆粒と、エタノールを添加せず本試験と同様
な方法で処理したフラクトオリゴ糖顆粒及び醗酵
乳顆粒とを5、10、15、20℃の各水温の水に投入
し、試験例1と同様にして溶解時間を測定した。
(表−2参照) 表−2に示す如くエタノールを2重量%以上添
加することにより最終製品である顆粒の水中での
溶解性が極めて著しく向上する。
[Table] As shown in Table 1, when the amount of water added to onion powder exceeds 2% by weight, the solubility of the resulting granules in water decreases. Test Example 2 To the same fructooligosaccharide powder as in Example 6 and fermented milk powder with a water content of 3% by weight, 1, 2, 3, 7, 10, and 20% by weight of pharmacopoeia absolute ethanol were added, respectively, at 25°C, RH 50%. It was mixed uniformly in the workshop.
After spreading the resulting mixture to a thickness of 0.2 cm, the temperature was 30°C.
The sample was left in an atmosphere of ℃ and RH 100% for 50 seconds, and the Aw was measured. (See Table 2) Each of the obtained granules was dried with ventilation at 50°C for 1 hour, and the fructooligosaccharide nodules with a moisture content of 1.5% by weight and the fermented milk nodules with a moisture content of 3% by weight were passed through a 10-mesh sieve. It was sized and granulated. The fructooligosaccharide granules and fermented milk granules obtained in this test and the fructooligosaccharide granules and fermented milk granules that had been treated in the same manner as in this test without adding ethanol were heated at various water temperatures of 5, 10, 15, and 20°C. It was poured into water and the dissolution time was measured in the same manner as in Test Example 1.
(See Table 2) As shown in Table 2, by adding 2% by weight or more of ethanol, the solubility of the final product granules in water is significantly improved.

【表】【table】

【表】 〈効 果〉 以上に述べた如く本発明によつて得られた吸湿
性粉末の顆粒はエタノール又は水含有エタノール
を混合した後圧力を加えることなく自然落下或は
自然放置の状態で加湿空気に接触せしめて粉体相
互に於ける多数接触点による付着を生じさせる
為、以降の乾燥工程に於けるエタノールの蒸散量
も少なくて回収装置も必要とせず、設備的にも本
発明による方法では従来の顆粒製造装置と何ら変
ることがない。 かくして得られた顆粒は従来開示されて来た技
術に比べ分散性、溶解性にすぐれている。
[Table] <Effects> As described above, the hygroscopic powder granules obtained by the present invention can be mixed with ethanol or water-containing ethanol and then allowed to fall naturally or left to humidify without applying pressure. Since the powders are brought into contact with air and adhesion is caused by multiple contact points with each other, the amount of ethanol evaporated in the subsequent drying process is small, and a recovery device is not required. There is no difference from conventional granule manufacturing equipment. The thus obtained granules have superior dispersibility and solubility compared to conventionally disclosed techniques.

Claims (1)

【特許請求の範囲】 1 吸湿性の低脂質粉末にエタノール又は水含有
エタノールを加え、賦形剤を使用することなく均
一に混合したのち、加湿空気に接触させ、顆粒化
することを特徴とする吸湿性粉末の顆粒製造方
法。 2 吸湿性の低脂質粉末に対し、2重量%〜20重
量%程度のエタノールを添加することを特徴とす
る特許請求の範囲第1項記載の吸湿性粉末の顆粒
製造方法。 3 吸湿性の低脂質粉末に添加するエタノール中
の水分量が吸湿性粉末に対して2重量%程度以下
であることを特徴とする特許請求の範囲第1項記
載の吸湿性粉末の顆粒製造方法。
[Claims] 1. Ethanol or water-containing ethanol is added to a hygroscopic low-lipid powder, mixed uniformly without using any excipients, and then brought into contact with humidified air to form granules. Method for producing granules of hygroscopic powder. 2. The method for producing granules of hygroscopic powder according to claim 1, characterized in that approximately 2% to 20% by weight of ethanol is added to the hygroscopic low-lipid powder. 3. The method for producing granules of hygroscopic powder according to claim 1, wherein the amount of water in the ethanol added to the hygroscopic low-lipid powder is about 2% by weight or less based on the hygroscopic powder. .
JP60178557A 1985-08-15 1985-08-15 Production of granule of moisture-absorbing powder Granted JPS6240278A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60178557A JPS6240278A (en) 1985-08-15 1985-08-15 Production of granule of moisture-absorbing powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60178557A JPS6240278A (en) 1985-08-15 1985-08-15 Production of granule of moisture-absorbing powder

Publications (2)

Publication Number Publication Date
JPS6240278A JPS6240278A (en) 1987-02-21
JPH0243468B2 true JPH0243468B2 (en) 1990-09-28

Family

ID=16050567

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60178557A Granted JPS6240278A (en) 1985-08-15 1985-08-15 Production of granule of moisture-absorbing powder

Country Status (1)

Country Link
JP (1) JPS6240278A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51149178A (en) * 1975-06-17 1976-12-21 Sumitomo Chem Co Ltd A process for production of granules
JPS5356332A (en) * 1976-10-30 1978-05-22 Kibun Kk Method of producing easy soluble fatty powder

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51149178A (en) * 1975-06-17 1976-12-21 Sumitomo Chem Co Ltd A process for production of granules
JPS5356332A (en) * 1976-10-30 1978-05-22 Kibun Kk Method of producing easy soluble fatty powder

Also Published As

Publication number Publication date
JPS6240278A (en) 1987-02-21

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