JPH0612985B2 - Dry food manufacturing method - Google Patents

Dry food manufacturing method

Info

Publication number
JPH0612985B2
JPH0612985B2 JP17860985A JP17860985A JPH0612985B2 JP H0612985 B2 JPH0612985 B2 JP H0612985B2 JP 17860985 A JP17860985 A JP 17860985A JP 17860985 A JP17860985 A JP 17860985A JP H0612985 B2 JPH0612985 B2 JP H0612985B2
Authority
JP
Japan
Prior art keywords
oil
pressure
treatment
water
product
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP17860985A
Other languages
Japanese (ja)
Other versions
JPS6240276A (en
Inventor
利光 北村
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.)
SANSEKI KIKAKU KK
Original Assignee
SANSEKI KIKAKU KK
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 SANSEKI KIKAKU KK filed Critical SANSEKI KIKAKU KK
Priority to JP17860985A priority Critical patent/JPH0612985B2/en
Priority to US06/910,140 priority patent/US4788072A/en
Priority to ES8600942A priority patent/ES2000188A6/en
Priority to EP86111277A priority patent/EP0212583B1/en
Priority to DE198686111277T priority patent/DE212583T1/en
Priority to DE8686111277T priority patent/DE3682725D1/en
Priority to CA000516060A priority patent/CA1303414C/en
Publication of JPS6240276A publication Critical patent/JPS6240276A/en
Publication of JPH0612985B2 publication Critical patent/JPH0612985B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は乾燥食品の製造方法、詳しくは果物、野菜類、
魚貝類等食品類を乾燥食品とする方法に関するもので、
得られた乾燥食品は、そのまま包装して食用に供する
か、又は必要に応じ更にこれを粉末化するなどして各種
加工食品製造用の原料に供することが出来るようにし
た。乾燥食品の製造方法を提供するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a method for producing a dry food, more specifically, fruits, vegetables,
It relates to the method of making foods such as fish and shellfish into dried foods,
The dried food thus obtained was packaged as it is for edible use, or if necessary, it was further powdered so that it could be used as a raw material for the production of various processed foods. A method for producing a dry food is provided.

〔従来の技術〕[Conventional technology]

従来この種の乾燥食品を得る方法としては真空フライ法
が知られている。この方法は例えばスライスした野菜等
の原料素材を糖液に6〜12時間浸漬し、これを真空釜
中で油により揚げてフライとした後引き上げて油を切る
方法である。この方法は浸漬処理時間及びフライ時間が
長く生産効率が悪いばかりでなくコスト的にも高くな
る。しかもフライ製品中の油分の残存量が多く(20〜
40%)、品質的に長期保存による劣化(油分の酸化)を
生じ異臭や味の低下等を起す欠点がある。また残油量が
多いので常温では粉末化することができない。更には素
材原料の本来の色相や風味が損なわれる。
Conventionally, a vacuum frying method has been known as a method for obtaining this type of dried food. In this method, for example, raw materials such as sliced vegetables are soaked in a sugar solution for 6 to 12 hours, fried in oil in a vacuum pot to make fries, and then pulled up to remove the oil. In this method, not only the immersion treatment time and the frying time are long but the production efficiency is poor, but also the cost is increased. Moreover, the amount of oil remaining in the frying products is large (20-
40%), there is a drawback in that the quality (deterioration of oil content) due to long-term storage causes a bad odor and deterioration of taste. Moreover, since the amount of residual oil is large, it cannot be pulverized at room temperature. Furthermore, the original hue and flavor of the raw material are impaired.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

本発明は上記のような従来法における欠点を改良したも
のである。すなわち、製造時間の短縮を図り、かつ、残
油量の著しい減少、原料素材の天然の色相や風味の保
持、品質劣化の防止、製品の加工性例えば粉末化等の容
易性、長期保存によるも品質の不変性等の性質を具備す
るすぐれた製品が得られる方法を提供するものである。
The present invention improves on the drawbacks of the conventional methods as described above. That is, the production time is shortened, and the amount of residual oil is remarkably reduced, the natural hue and flavor of the raw material are retained, quality deterioration is prevented, the processability of the product is easy, for example, pulverization, and long-term storage is also possible. It is intended to provide a method for obtaining an excellent product having properties such as quality invariance.

〔問題点を解決するための手段〕[Means for solving problems]

すなわち本発明は、水洗した食品原料素材を必要な形態
にスライス又は切断し、塩水、酸、糖類など所要の浸透
溶媒液中に浸漬又はブランチング処理した後、該素材を
加圧、減圧可能な釜内のかご中に収容し、かごを回転さ
せつつ所要の浸透液及び油脂を噴霧し、次いで水蒸気加
圧を行つた後急激に減圧状態とし、このような加圧と急
激な減圧とを適宜反復した後最後に減圧下で、かごを高
速回転せしめて素材中の水分及び油分を分離、除去する
ことを特徴とする乾燥所品の製造方法である。
That is, the present invention, after slicing or cutting the water-washed food material raw material into a required form, dipping or blanching in a required permeation solvent liquid such as salt water, acid, or sugar, the material can be pressurized or depressurized. It is housed in a car in a kettle, and while the car is rotating, the required penetrant and fats and oils are sprayed, and then steam pressure is applied, followed by a sudden depressurization state. After repeating, finally, the basket is rotated at a high speed under reduced pressure to separate and remove water and oil in the raw material, which is a method for producing a dry product.

本発明において適用できる乾燥用材料としては各種野菜
類、果物類、魚貝類等があげられ、目的とする乾燥後の
製品形状に応じた形態に切断するが、特に切断の必要の
ない場合は原形のままでもよい。しかしながら切断処理
を施せば浸透溶媒処理が効果的に行なわれる。浸透溶媒
液としては例えば食塩、クエン酸又はリンゴ酸、糖類、
アルコール類その他各種のものが、素材及び用途に応じ
て選択使用でき、特に限定されるものではない。浸漬処
理時間は通常30分〜1時間の浸漬静置でよい。この浸
漬によつて素材中の組織細胞より水分がかなり抽出され
る。特に塩水又は酸水溶液でブランチング処理したもの
は後処理を施して乾燥製品化した時、果物、野菜類など
天然のそれぞれの色相をあざやかに保持うることができ
る。上記の浸漬処理した素材を加圧、減圧可能な釜内の
網かごの中に入れて回転しながら浸漬溶媒液、油脂等を
それぞれのノズルから噴霧し、水蒸気圧によつて浸透圧
力0〜10Kg/Hgの範囲で素材の所要条件に合わせて加
熱加圧を行なつて浸透せしめ、次いで所定圧力に達する
と同時に、釜の自動開閉弁を作動させて瞬間的に釜内を
例えば30〜5mm/Hgに減圧状態とし、これを反復操作す
る。なおこの際網かごの回転も適宜調節する。容器内の
圧力を高めると、収容されている素材の組織が弛緩さ
れ、含有水分が外部に出やすい状態になると共に加熱用
の油脂は内部に入り易くなる。したがって、加圧下で加
熱された油脂を噴射すると油脂は速やかに材料の組織内
に浸透するので、効率よく素材の深部まで必要な熱を与
えることができる。そこで急激に減圧すると、素材中の
水分及び浸透した油脂は短時間に素材内から排出されて
乾燥が行われる。素材の脱水状態をコントロールし乍ら
反復し、必要な乾燥状態に達した時減圧状態下で網かご
に高速回転を与えて、水分及び油分を分離除去せしめ
る。なお本発明において使用する油脂としては例えばパ
ーム油、ライス油、綿実油、ラード等があげられ必要に
応じて適宜調合したものなどが使用される。
Examples of the drying material applicable in the present invention include various vegetables, fruits, fish and shellfish, etc., which are cut into a shape according to the intended dried product shape, but if it is not particularly necessary to cut, the original shape is used. You can leave it as it is. However, if the cutting treatment is applied, the permeation solvent treatment is effectively performed. Examples of the osmotic solvent liquid include salt, citric acid or malic acid, sugar,
Alcohols and various other substances can be selected and used according to the material and application, and are not particularly limited. Immersion treatment time is usually 30 minutes to 1 hour. By this immersion, a considerable amount of water is extracted from the tissue cells in the material. In particular, those subjected to a blanching treatment with salt water or an aqueous acid solution can retain their respective natural hues such as fruits and vegetables when they are post-treated to give a dried product. Put the above-mentioned dipping-treated material in a net basket in a pot capable of pressurizing and depressurizing, and spray the dipping solvent liquid, oil and fat, etc. from each nozzle while rotating, and the osmotic pressure of 0 to 10 kg by steam pressure. In the range of / Hg, heating and pressurization are performed according to the required conditions of the material to infiltrate, and then at the same time when a predetermined pressure is reached, the automatic on-off valve of the kettle is activated to instantaneously move the inside of the kettle to, for example, 30 to 5 mm / Reduce the pressure to Hg and repeat this operation. At this time, the rotation of the net cage is also adjusted appropriately. When the pressure in the container is increased, the tissue of the contained material is relaxed, the contained water is easily discharged to the outside, and the heating oil and fat is easily introduced into the inside. Therefore, when the oil / fat heated under pressure is injected, the oil / fat quickly penetrates into the tissue of the material, and the necessary heat can be efficiently applied to the deep part of the material. Then, when the pressure is rapidly reduced, the moisture in the material and the permeated fats and oils are discharged from the material in a short time and dried. The dehydration state of the material is controlled and repeated. When the required dry state is reached, the net basket is rotated at high speed under a reduced pressure to separate and remove water and oil. The oils and fats used in the present invention include, for example, palm oil, rice oil, cottonseed oil, lard and the like, which are appropriately blended if necessary.

このようにして得られた乾燥物は、用途に応じ、そのま
ま製品として包装するか、或は粉末化して、製菓用、そ
の他種々の加工食品類の製造原料に供する。本発明によ
る乾燥品は天然の風味、色相を保持するばかりでなく保
存性もよく、かつ粉末加工もし易いものである。
The dried product thus obtained is packaged as it is as a product or powdered to be used as a raw material for confectionery and other various processed foods, depending on the intended use. The dried product according to the present invention not only retains the natural flavor and hue, but also has good storability and is easily powder-processed.

実施例1 市販の玉ねぎを洗浄及び脱皮し芯取り及び四ツ切りを行
ない、塩水(塩度3〜20%)に浸漬(10〜30分
間、温度40〜60℃)する。
Example 1 Commercially available onions are washed and dehulled, cored and cut into four pieces, and immersed in salt water (salinity 3 to 20%) (10 to 30 minutes, temperature 40 to 60 ° C).

加圧減圧容器の網カゴの中に前記の浸漬素材を水洗後入
れる。一方浸透溶液(糖類・マルトース・デキストリン
・コーンスターチ、濃度20〜50)をノーズルにて噴
霧する。その場合、中のカゴ体をゆるやかな回転をさせ
ながらさらに水蒸気を吹き込み加圧化(1〜7Kg/Hg)
とする。
The above immersion material is put into a net basket of a pressurization / decompression container after washing with water. On the other hand, a penetrating solution (sugar, maltose, dextrin, corn starch, concentration 20 to 50) is sprayed with a nose. In that case, steam is blown and pressure is applied (1-7 Kg / Hg) while gently rotating the basket inside.
And

温度60〜80℃に加熱した綿実油又はパーム核油をノ
ズルにて上記加圧容器中に噴霧状に吹き込むと、容器内
で水蒸気と混合し微細な泡沫状態となる。器内の圧力が
4Kg/Hgに達した時点で、自動調節弁を開放して5
〜20Torrに減圧する。この減圧状態で3〜5分経
過後再び自動調節弁を閉じ、前回の加圧状態で操作し、
再び減圧状態とする。10〜20分後糖液及び蒸気を中
止し、油脂のみを約3〜5分間後に中止する。さらにカ
ゴ体を高速回転5分間後に停止し、常圧にもどしてカゴ
体を取り出す。なお、前記油脂を含む微細な泡抹は器外
に油脂タンクに返還されて再使用に供される。
When cottonseed oil or palm kernel oil heated to a temperature of 60 to 80 ° C. is blown into the above pressurized container with a nozzle in a spray form, it mixes with water vapor in the container and becomes a fine foam state. When the pressure inside the vessel reaches 4 Kg / Hg, open the automatic control valve to
Reduce pressure to -20 Torr. In this depressurized state, after 3 to 5 minutes have passed, the automatic control valve is closed again, and the previous pressurization state is used.
The pressure is reduced again. After 10 to 20 minutes, the sugar solution and steam are stopped, and only the oil and fat is stopped after about 3 to 5 minutes. Further, the basket body is stopped after 5 minutes of high-speed rotation, returned to normal pressure, and the basket body is taken out. It should be noted that the fine foam particles containing the oil and fat are returned to the oil and fat tank outside the container for reuse.

こうして得ることができた乾燥製品は、油分5%以下、
水分1%以下、フレーバー色等優れたものであつた。
The dry product thus obtained has an oil content of 5% or less,
The water content was 1% or less, and the flavor color was excellent.

実施例2 (1)品種:キヤロツト・カボチヤ・タケノコ・ゴボウ (2)処理条件 脱皮及びスライス ブランチング処理:食塩水(濃度20〜30%、温度
60〜80℃)に30分〜1時間、その後急冷(−18
〜−30℃) 浸透溶媒:マルトース・コーンスターチ混合溶液(濃
度10〜30%、温度60℃) 浸透圧:6〜7Kg/Hg その他の条件は前実施例1と同一とする。
Example 2 (1) Variety: Kyarotsu, Cabocha, Takenoko, Burdock (2) Treatment conditions Hulling and slicing Blanching treatment: Saline (concentration 20-30%, temperature 60-80 ° C) for 30 minutes-1 hour, then Rapid cooling (-18
˜−30 ° C.) Penetration solvent: Maltose / corn starch mixed solution (concentration 10 to 30%, temperature 60 ° C.) Osmotic pressure: 6 to 7 Kg / Hg Other conditions are the same as those in Example 1 above.

上記の条件により得られた乾燥製品は、油分5%以下水
分1%以下であり、それらの原料素材本来の色調と香味
を有し、ポーラスなクリスプの優れたものであつた。
The dried product obtained under the above conditions had an oil content of 5% or less and a water content of 1% or less, had the original color tone and flavor of those raw materials, and had an excellent porous crisp.

実施例3 (1)品種:ホウレンソウ・ダイコン葉・ピーマン・サヤ
インゲン・キヌサヤ・アスパラ (2)処理条件 ピーマンのみ4つ切り ブランチング処理:食塩水(濃度20〜30%、温度
90℃)に1分以内、その後急冷(−18〜−30℃) 浸透溶媒:マルトース・デキストリン・コーンスター
チ濃度30%、温度20℃、40% 浸透圧:4Kg/Hg以内 その他の条件は実施例1と同一とする。
Example 3 (1) Variety: Spinach, Japanese radish leaf, green pepper, green beans, quinusaya, asparagus (2) Treatment condition Cut only four bell peppers Blanching treatment: Saline (concentration 20-30%, temperature 90 ° C) for 1 minute Within, then rapidly cooled (-18 to -30 ° C) Penetration solvent: Maltose / dextrin / corn starch concentration 30%, temperature 20 ° C, 40% Osmotic pressure: within 4 Kg / Hg Other conditions are the same as in Example 1.

得られた乾燥製品は、各々の原料素材本来の色調・香味
を有し、ポーラスなクリスプの優れた製品であつた。
The obtained dried product had the original color tone and flavor of each raw material, and was an excellent product with a porous crisp.

実施例4 (1)品種:リンゴ・カキ・ナシ・キウイ・メロン・スイ
カ・バナナ・イチゴ (2)処理条件 脱皮及びスライス 浸漬:バナナのみ酸処理、リンゴ酸(濃度3%以内、
30分〜1時間)、その他は食塩水(濃度20〜30
%、30分〜1時間)その後水洗 浸透溶媒:マルトース・コーンスターチ混合溶液(濃
度10〜30%、温度60℃) 浸透圧:6〜7Kg/Hg その他の条件は実施例1と同一とする。
Example 4 (1) Varieties: apple, oyster, pear, kiwi, melon, watermelon, banana, strawberry (2) Treatment conditions molting and slicing Immersion: acid treatment of banana only, malic acid (concentration within 3%,
30 minutes to 1 hour), others are saline (concentration 20 to 30)
%, 30 minutes to 1 hour) and then washed with water Penetration solvent: Maltose / corn starch mixed solution (concentration 10 to 30%, temperature 60 ° C.) Osmotic pressure: 6 to 7 kg / Hg Other conditions are the same as in Example 1.

上記の条件により得られた乾燥製品は、油分10%以下、
水分1%以下であり、素材の色調・香味等を有するテク
スチヤーの乾燥製品であつた。
The dry product obtained under the above conditions has an oil content of 10% or less,
The water content was 1% or less, and the product was a dry textured product having the color tone and flavor of the material.

実施例5 (1)品種:ウメボシ・ニンニク・干ブドウ (2)処理条件 脱皮及びスライス(ニンニクのみ) ブランチング処理:リンゴ酸(濃度3%以内)で、ニ
ンニクのみ90℃で5分以内、その他は60℃以下で3
0分〜1時間、その後急冷(−18〜−30℃) 浸透溶媒:マルトース、コーンスターチ混合溶液(濃
度10〜30%温度60℃) 浸透圧:7Kg/Hg その他の条件は実施例1と同一とする。
Example 5 (1) Variety: Umeboshi, garlic, dried grapes (2) Treatment conditions Hulling and slicing (garlic only) Blanching treatment: Malic acid (within 3% concentration), garlic only at 90 ° C. within 5 minutes, and others Is 3 at below 60 ° C
0 minutes to 1 hour, followed by rapid cooling (-18 to -30 ° C) Permeation solvent: Maltose, corn starch mixed solution (concentration 10 to 30%, temperature 60 ° C) Osmotic pressure: 7 Kg / Hg Other conditions are the same as in Example 1. To do.

上記の条件により得られた乾燥製品は、特にポーラスな
クリスプの、また味・色調などの優れた乾燥製品であつ
た。
The dried product obtained under the above conditions was a particularly dry product having a porous crisp and an excellent taste and color tone.

実施例6 (1)品種:イワシ・ウルメ・ワカサギ・エビ・イカ・カ
ニ・イリコ・ホタテ貝・真珠貝・魚肉ソーセージ (2)処理条件 食塩をふりかけ混ぜる(30分〜1時間)その後水洗 浸透圧4Kg/Hg以内、但し、ホタテ貝・エビ・イカ類
は圧力7〜8Kg/Hg 油脂温度:60〜120℃ その他の条件は実施例1と同一とする。
Example 6 (1) Variety: sardines, ume, smelt, shrimp, squid, crab, irico, scallop, pearl shell, fish meat sausage (2) Treatment conditions Sprinkle salt (30 minutes to 1 hour) and then wash with water Osmotic pressure Within 4 Kg / Hg, except for scallop, shrimp and squid, pressure is 7 to 8 Kg / Hg Oil and fat temperature: 60 to 120 ° C. Other conditions are the same as in Example 1.

上記条件における乾燥製品において、エビ・イカ・ホタ
テ貝は水分4〜6%、油分5〜10%であり、それぞれ
鮮やかな色調で、素材の香味が優れた乾燥製品が得られ
る。
Among the dried products under the above conditions, the shrimp, squid, and scallop have a water content of 4 to 6% and an oil content of 5 to 10%, and each has a vivid color tone and is excellent in the flavor of the material.

実施例7 (1)品種:ハム・ソーセージ・肉類 (2)処理条件 事前に食塩・コーンスターチ・マルトースを使用して
ロール加工する。
Example 7 (1) Variety: ham, sausage, meat (2) Processing conditions Roll processing is performed in advance using salt, corn starch and maltose.

浸透圧7〜8Kg/Hg 油脂温度60〜120℃ その他の条件は実施例1と同一とする。Osmotic pressure 7 to 8 kg / Hg Oil and fat temperature 60 to 120 ° C. Other conditions are the same as in Example 1.

上記条件における乾燥製品は、従来にないすぐれた色調
と香味の乾燥製品であつた。
The dried product under the above conditions was a dried product having an excellent color tone and flavor which has never been obtained.

発明の効果 本発明の浸透圧処理応用の乾燥食品の製造方法(3)を従
来の真空凍結乾燥方法(1)又は真空フライ乾燥方法(2)と
対比すると、生産効率与は品質等において、次に示すと
おり、本発明の製法による効果は極めて大きいものであ
る。すなわち、 野菜類又は果物類、或いは魚貝類等の処理時間内にお
いて (1)凍結・乾燥処理時間 8〜16時間 (2)真空フライ処理時間 6〜13時間(浸漬時間含む) (3)浸透乾燥処理時間 2〜6時間(浸漬時間含む) 上記のとおり、本発明の浸透圧力処理乾燥方法において
は、乾燥所品製造処理時間が大きく短縮され、又1サイ
クル処理量が大きく従来にない生産効率となり、他の数
倍向上しコスト的にも充分な効果が得られる。
Effect of the invention When the method for producing a dry food (3) for application of the osmotic pressure treatment of the present invention is compared with the conventional vacuum freeze-drying method (1) or the vacuum frying drying method (2), the production efficiency is in terms of quality, etc. As shown in, the effect of the manufacturing method of the present invention is extremely large. That is, within the processing time of vegetables or fruits, or fish and shellfish, etc. (1) Freezing / drying processing time 8 to 16 hours (2) Vacuum frying processing time 6 to 13 hours (including immersion time) (3) Permeation drying Treatment time 2 to 6 hours (including immersion time) As described above, in the osmotic pressure treatment drying method of the present invention, the drying product production processing time is greatly shortened, and one cycle processing amount is large, resulting in unprecedented production efficiency. However, it is several times better than the others, and a sufficient effect can be obtained in terms of cost.

本発明は浸透圧処理において、まず食塩水や酸又は多
糖類等でしかも加圧減圧の急速・短時間処理をなすた
め、従来の真空凍結乾燥や真空フライ等と製品品質を比
較した場合、優れた天然素材の鮮やかな色彩や風味など
を有しかつ長期保存が可能となる。
The present invention, in the osmotic pressure treatment, first performs rapid and short-time pressure reduction and pressure reduction with salt solution, acid, or polysaccharide, etc., so when comparing product quality with conventional vacuum freeze drying, vacuum frying, etc., it is excellent. It has the bright colors and flavors of natural materials and can be stored for a long period of time.

また本発明の浸透圧乾燥処理においては油脂類(硬化
油)を噴霧又は減圧高速遠心分離処理するために、従来
の常圧フライや真空フライ処理等に対比した場合、下記
表の如く製品の残油量が特に少なく、従つて製品品質に
おいて残油成分の劣化(酸化過酸物価)による味,臭
い,色相などの品質変化がなく、長期間安定性を保持す
ることができる。
Further, in the osmotic pressure drying treatment of the present invention, in order to spray oil or fat (hardened oil) or perform high-speed centrifugal separation under reduced pressure, when compared with conventional atmospheric pressure frying or vacuum frying, etc., the product remains as shown in the table below. Since the amount of oil is particularly small, there is no change in quality such as taste, odor and hue due to deterioration of residual oil component (oxidized peracid value) in product quality, and stability can be maintained for a long time.

本発明の浸透圧乾燥処理と、従来の処理方法とを、製品
品質について、含油分又は含水分等更に含油分中の酸化
・過酸化物価等に関して比較試験を行なつた結果、上記
表の如く従来にない優れた効果が発揮された。
The osmotic pressure drying treatment of the present invention and the conventional treatment method were subjected to a comparative test with respect to the product quality regarding the oil content, the water content, etc., and the oxidation / peroxide value, etc. in the oil content, as shown in the above table. The outstanding effect which was not existed before was demonstrated.

また本発明における浸透圧乾燥方法は、特に処理温度
(40〜70℃)処理乾燥時間(30分〜1時間)にお
いて低温急速乾燥処理が可能なため、原料素材の栄養成
分が破壊されず、又水分除去されるために濃縮化され高
濃度な健康食品加工として優れた効果をもたらす。
Further, the osmotic pressure drying method of the present invention can perform low-temperature rapid drying treatment especially at the treatment temperature (40 to 70 ° C.) and the treatment drying time (30 minutes to 1 hour), so that the nutritional components of the raw material are not destroyed, and It is concentrated because it removes water and has an excellent effect as a high-concentration health food processing.

更に本発明の浸透圧乾燥方式で処理した製品は、油脂
(融点30〜45℃)の残油分が非常に少なく、又天然
素材の色相がそのままであるために更に粉末加工するこ
とが可能となり、優れた色彩と香味のパウダーの製品化
を得ることができ、各種加工食品原料として好適であ
る。
Further, the product treated by the osmotic pressure drying method of the present invention has a very small amount of residual oil of fats and oils (melting point: 30 to 45 ° C.), and since the hue of the natural material is the same, further powder processing becomes possible, It is possible to obtain powder with excellent color and flavor, and it is suitable as a raw material for various processed foods.

例えば前述の浸透圧乾燥品を粉末処理したパウダーを使
用し、製菓関係(クツキー・せんべい・和菓子・米菓・
その他)や又アイスクリーム或いはハム・ソーセージ等
の基材に使用することによつて、従来法では得られなか
つた天然の香味・色彩等などを有する優れた製品化が可
能であり、本発明の効果は極めて大きいものである。
For example, using powder obtained by powder-processing the above-mentioned osmotic pressure dried product, confectionery-related products (Kutsky, rice cracker, Japanese confectionery, rice confectionery,
Others), or by using it as a base material for ice cream, ham, sausage, etc., it is possible to produce an excellent product having a natural flavor, color, etc. which could not be obtained by the conventional method. The effect is extremely large.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】水洗した食品原料素材を必要な形態にスラ
イス又は切断し、塩水、酸又は糖類など所要の浸透溶媒
液中に浸漬又はブランチング処理した後、該素材を加
圧、減圧可能な釜内のかご中に収容し、かごを回転させ
つつ所要の浸透液及び油脂を噴霧し、次いで水蒸気加圧
を行つた後急激に減圧状態とし、このような加圧と急激
な減圧とを適宜反復した後最後に減圧下で、かごを高速
回転せしめて素材中の水分及び油分を分離、除去するこ
とを特徴とする乾燥食品の製造方法。
1. A slicing or cutting of a food raw material that has been washed with water into a required form, and immersing or blanching in a required permeation solvent liquid such as salt water, acid or saccharide, and then pressurizing or depressurizing the material. It is housed in a car in a kettle, and while the car is rotating, the required penetrant and fats and oils are sprayed, and then steam pressure is applied, followed by a sudden depressurization state. A method for producing a dry food, characterized in that after repeating, finally, a basket is rotated at a high speed under reduced pressure to separate and remove water and oil in the material.
JP17860985A 1985-08-15 1985-08-15 Dry food manufacturing method Expired - Lifetime JPH0612985B2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP17860985A JPH0612985B2 (en) 1985-08-15 1985-08-15 Dry food manufacturing method
US06/910,140 US4788072A (en) 1985-08-15 1986-07-30 Method of dehydrating foods
ES8600942A ES2000188A6 (en) 1985-08-15 1986-08-08 Method of manufacturing dried food and plant products.
EP86111277A EP0212583B1 (en) 1985-08-15 1986-08-14 Method of manufacturing dried food and plant products
DE198686111277T DE212583T1 (en) 1985-08-15 1986-08-14 METHOD FOR PRODUCING DRY FOOD AND PLANT PRODUCTS.
DE8686111277T DE3682725D1 (en) 1985-08-15 1986-08-14 METHOD FOR PRODUCING DRY FOOD AND PLANT PRODUCTS.
CA000516060A CA1303414C (en) 1985-08-15 1986-08-15 Process for dehydrating food products

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17860985A JPH0612985B2 (en) 1985-08-15 1985-08-15 Dry food manufacturing method

Publications (2)

Publication Number Publication Date
JPS6240276A JPS6240276A (en) 1987-02-21
JPH0612985B2 true JPH0612985B2 (en) 1994-02-23

Family

ID=16051443

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17860985A Expired - Lifetime JPH0612985B2 (en) 1985-08-15 1985-08-15 Dry food manufacturing method

Country Status (1)

Country Link
JP (1) JPH0612985B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0650484U (en) * 1992-12-17 1994-07-12 株式会社サンワ福岡 Pressurization / depressurization device

Also Published As

Publication number Publication date
JPS6240276A (en) 1987-02-21

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