JP3653354B2 - How to dry food - Google Patents

How to dry food Download PDF

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JP3653354B2
JP3653354B2 JP28629796A JP28629796A JP3653354B2 JP 3653354 B2 JP3653354 B2 JP 3653354B2 JP 28629796 A JP28629796 A JP 28629796A JP 28629796 A JP28629796 A JP 28629796A JP 3653354 B2 JP3653354 B2 JP 3653354B2
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drying
food
moisture
dried
fresh
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JPH10127263A (en
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清川  晋
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清川 晋
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  • Freezing, Cooling And Drying Of Foods (AREA)
  • Storage Of Fruits Or Vegetables (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、野菜、魚介類等の乾燥食品を製造するための食品の乾燥方法に関し、とくに食品の変質、変色等を防いで乾燥を行うための乾燥方法に関する。
【0002】
【従来の技術】
生鮮食品の乾燥方法として、天日乾燥、熱風乾燥、赤外線乾燥、凍結乾燥など各種の方法があるが、比較的低温度で迅速に乾燥できる方法として、近年減圧乾燥法が注目されている。
【0003】
減圧乾燥法は乾燥室内を減圧にすることにより水分の蒸発速度を大きくし、室温に近い温度例えば50℃以下で乾燥することにより、食品成分の分解や食品の変質、変色を防いで、元の食品の風味を残した乾燥食品を得る方法として優れている。
【0004】
しかし、減圧乾燥法によっても食品の乾燥を完了するまでに相当の長時間を要し、このために雑菌の繁殖や食品成分の酸化が起こって、元の生鮮食品の風味を残す上で必ずしも十分と云えない。
【0005】
さらに、元の食品の風味を残して乾燥する別の方法として、真空凍結乾燥法がある。これは、被乾燥物を0〜−40℃に冷却して凍結した後、真空乾燥室内で凍結状態のまま水分を気体として除去する乾燥方法で、乾燥室内の圧力を固体の水分の蒸気圧以下にするため、絶対圧でたとえば水柱50mm(0.5kPa)程度以下の高真空にする必要がある。
【0006】
真空凍結乾燥法は、近年インスタント食品例えば即席麺、お茶漬、ふりかけ、スープ類等の具材や調味素材の乾燥方法として多用されるようになってきた。これは一旦煮沸調理した素材を乾燥するもので、乾燥工程での雑菌の侵入・繁殖を防止でき、長期保存に適するという利点を有する。また、生鮮食品、例えば野菜、肉類、魚介類等を直接真空凍結乾燥して、長期保存可能な乾燥食品を製造することも試みられるようになってきた。
【0007】
しかし、真空凍結乾燥法は乾燥速度がきわめておそく、食品中の水分を全てこれで除こうとすると乾燥時間が極端に長くなり、そのため乾燥コストが著しく大きくなるという問題がある。
【0008】
【発明が解決しようとする課題】
本発明は、上記のような従来の食品の乾燥方法の問題点に鑑み、より良く元の食品の風味を残し、長期保存可能でありかつ比較的乾燥コストの低い食品の乾燥方法を提供することを目的とする。
【0009】
とくに、減圧乾燥法その他従来の室温付近での乾燥法と真空凍結乾燥法とを適切に組み合わせることにより、食品の変質防止と乾燥コストの低減という二つの目的を両立させうる食品の乾燥方法を提供することを目的とする。
【0010】
【課題を解決するための手段】
本発明の発明者らは、従来の乾燥方法、例えば40℃以下で減圧下で乾燥する方法(以下、「常温減圧乾燥法」という)及び真空凍結乾燥法における各種生鮮食品の乾燥速度について検討し、模式的に図3に示すような関係があることを見出した。
【0011】
すなわち、常温減圧乾燥法は初期の乾燥速度は大きいが、食品中の水分が生鮮状態の20〜30%程度になると乾燥速度が低下し始め、とくに生鮮状態の水分の15〜20%以下になるとほとんど乾燥が進行しなくなって、なかなか最終乾燥水分(生鮮状態の水分の3〜10%程度)に到達しない。
【0012】
一方、真空凍結乾燥法では初期の乾燥速度は非常に小さいが、食品中の水分が生鮮状態の20〜30%以下になっても、乾燥速度はあまり低下せず最終乾燥水分に到達する。
【0013】
このように低水分域で乾燥速度に差が生じる理由は、以下のように考えられる。すなわち、常温減圧乾燥法においては、乾燥の初期は主に食品組織中の自由水(食品組織と結合していない水分)が蒸発するため乾燥速度が大きい。一方低水分域では主に食品組織に多分子層に付着・結合した水分が蒸発するようになるが、この水分は食品組織との親和力が大きくそのため蒸発速度は著しくおそくなる。
【0014】
これに対して真空凍結乾燥法においては、上記のような食品組織に多分子層に付着・結合した水分は、凍結して自由水と一緒に固体の水分となり、食品組織との親和力がほとんど失われる。これが真空凍結乾燥法において、低水分域(生鮮状態の水分の20〜30%以下)でも乾燥速度が低下しない理由と考えられる。
【0015】
本発明の発明者らは、上記のような食品の乾燥挙動に着目し、非凍結乾燥と凍結乾燥を適切に組合せることによって、食品の変質が少なくかつ効率の良い乾燥が可能なことを見出した。
【0016】
本発明は上記の知見に基いてなされたもので、その要旨は、
(1)生鮮食品又はこれを煮沸調理した食品を乾燥するに際して、被乾燥物中の水分が生鮮状態の水分の10〜30%になるまで被乾燥物の温度を10〜40℃として予備乾燥した後、真空凍結乾燥することを特徴とする食品の乾燥方法である。
【0017】
(2)また、前記予備乾燥を、大気圧から水柱−30mm〜−200mmの減圧下で行うことを特徴と前項(1)記載の食品の乾燥方法である。
【0018】
【発明の実施の形態】
本発明において、被乾燥物たる食品としては、例えば、にんじん、じゃがいも、かぼちゃ、ねぎ、ほうれん草等の生鮮野菜類、鮭、鯛、鰈、いか、えび、ほたて等の生鮮魚介類、生鮮肉類又はこれらを煮沸調理した食品等があげられる。
【0019】
本発明の食品の乾燥方法においては、まず被乾燥物が凍結しない温度すなわち0℃以上の温度で予備乾燥し、次いで真空凍結乾燥するが、予備乾燥後の被乾燥物中の水分を生鮮状態の水分の10〜30%の範囲内とすることを特徴とする。
【0020】
以下、予備乾燥後の水分をこの範囲に限定する理由について説明する。
被乾燥物の水分が生鮮状態の水分の30%より高い状態で真空凍結乾燥を行うと、食品の組織中に数百μmから数mmの氷片が生じる。この氷片が蒸発した後には空孔が残るため、このような空孔の生じた乾燥食品を水に戻しても、元の生鮮状態の食感や歯ごたえが得られず、食品としての風味が著しく低下する。
【0021】
本発明者らは、いずれの食品においても、生鮮状態の水分の30%以下から真空凍結乾燥すれば、このような空孔の生成による風味の低下がほとんど無いことを知見した。したがって、本発明においては、予備乾燥後の被乾燥物中の水分を生鮮状態の水分の30%以下とする。
【0022】
また、本発明者らの知見によれば、予備乾燥(非凍結状態での乾燥)においては、被乾燥物中の水分が生鮮状態の20〜30%以下で乾燥速度が低下し始め、生鮮状態の水分の10%近くになると乾燥速度の低下が著しくなる。
【0023】
このため、被乾燥物中の水分が生鮮状態の10%より低くなるまで予備乾燥すると、乾燥時間が過大になり、雑菌の繁殖等による食品の変質のおそれがあって好ましくない。したがって、本発明においては予備乾燥後の被乾燥物中の水分を生鮮状態の水分の10%以上とする。なお、食品の変質をより完全に防止するという観点からは、予備乾燥後の被乾燥物中の水分をより高い値、例えば生鮮状態の水分の15%以上にとどめることが好ましい。
【0024】
予備乾燥(非凍結状態での乾燥)における低水分域での乾燥速度の低下のしかたは、食品の種類によって相違する。したがって、各食品について予備乾燥及び真空凍結乾燥の速度を測定して、前者が後者より遅くなる被乾燥物中の水分の値を予め把握し、この水分の値付近で予備乾燥から真空凍結乾燥に移行すれば、全体の乾燥時間を最も短縮することができる。
【0025】
本発明において、予備乾燥から真空凍結乾燥に移行する水分を生鮮状態の水分を基準に定めるのは、本発明者らの検討結果から、生鮮食品のみならずこれを煮沸調理した食品の大部分についても、乾燥速度の低下や氷片による食品組織中の空孔の生成が起こる水分の値が、生鮮状態の水分を基準に表示できることが知見されたためである。
【0026】
なお、ここでいう生鮮状態とは、農産物、海産物等を採取してから生鮮物として市場で取引されうる状態で、通常野菜類は80〜95重量%、魚介類は60〜80重量%程度の水分を含んでいる。
【0027】
請求項1記載の本発明においては、予備乾燥の条件は被乾燥物の温度が10〜40℃であればよく、乾燥の方法もとくに限定されない。天日乾燥、冷風乾燥、赤外線加熱乾燥等の各種の方法を適用でき、乾燥時の雰囲気の圧力も大気圧でも減圧下であってもよい。
【0028】
また、真空凍結乾燥の方法及び条件もとくに限定する必要はなく、通常の方法例えば、被乾燥物を0〜−40℃で凍結させた後、氷点下の真空室(絶対圧力が例えば水柱50mm以下)内に封入して所定時間乾燥するような方法によればよい。
【0029】
請求項2記載の本発明においては、大気圧から水柱−30mm〜−200mmの減圧下で予備乾燥を行い、被乾燥物の水分が生鮮状態の水分の10〜30%になった後、真空凍結乾燥することを特徴とする。
【0030】
減圧下で予備乾燥を行う理由は、室温又はこれに近い低い温度での乾燥速度を大きくするためである。この場合、減圧度が大きい方が乾燥速度は大きくなるが、反面乾燥設備が高価になって好ましくない。後の実施例に示すような、乾燥室へ給気しつつ同時に室内の湿分の高い空気を排気する乾燥システムによれば、乾燥室内は軽度の減圧例えば水柱−30mm〜−200mm程度の減圧で、十分乾燥速度を大きくすることができる。
【0031】
また、請求項2の本発明の予備乾燥においては、乾燥室内に加熱手段例えば赤外線ヒーターと被乾燥物の温度測定手段例えば輻射熱温度センサーを設置することが好ましい。このような構成をとることにより、確実に被乾燥物の温度を10〜40℃に制御して予備乾燥を行うことができる。
【0032】
請求項2の発明において、予備乾燥中の被乾燥物の温度の上限を40℃とするのは、これ以上では食品中の酵素の働き等による食品の変質や有用成分の分解等が避け難くなるためである。また、被乾燥物の温度の下限を10℃とするのは、これ以下では減圧下でも乾燥速度がおそくなり過ぎ、効率的な乾燥が困難になるためである。
【0033】
また、乾燥室内に紫外線照射装置を設置して、所定時間或いは定期的に紫外線を被乾燥物に照射することにより、雑菌等を死滅させることも可能である。なお、請求項2の本発明においても、真空凍結乾燥の条件及び方法はとくに限定する必要はなく、通常の方法によればよい。
【0034】
本発明においては、被乾燥物の水分が生鮮状態の10〜30%になったところで予備乾燥を終了し真空凍結乾燥に移行するが、この移行時点を調整する方法としては、例えば▲1▼予め所定の乾燥条件で乾燥時間と被乾燥物中の水分の関係を測定しておき、乾燥時間を規定する方法、▲2▼乾燥中に連続的又は定期的に被乾燥物の重量を測定し、重量減から水分変化を判定して移行する方法、等の各種の方法によることができる。
【0035】
【実施例】
にんじん、かぼちゃ、やまといも等の生鮮野菜を、給・排気手段と赤外線ヒーターを有する乾燥室内で減圧下で予備乾燥した後、真空凍結乾燥する本発明の食品の乾燥方法を実施した。
【0036】
実施例は、予備乾燥で被乾燥物中の水分を生鮮状態の約20%にした後、真空凍結乾燥した場合である。
【0037】
予備乾燥においては被乾燥物の温度は40℃、乾燥室の雰囲気圧力は水柱−50mmの減圧とし、約10時間予備乾燥した。その後、被乾燥物を−15〜20℃で凍結し、氷点下の真空タンク内で絶対圧0.1kPa以下の真空下で約15時間真空凍結乾燥した。最終乾燥水分は生鮮状態の3〜5%であった。
【0038】
一方、比較例1は減圧下で凍結しない温度で最終乾燥水分まで乾燥した場合で、上記の予備乾燥と同じ条件で約40時間乾燥を行った。比較例2は生鮮状態から直ちに真空凍結乾燥を行った場合で、上記と同じ条件で約60時間真空凍結乾燥した。なお、比較例2においては、上記の時間内では最終乾燥水分には到達しなかった。
【0039】
図1に、にんじんを乾燥した場合の実施例及び比較例1、2における乾燥時間と食品中の水分の関係を示す。図に見られるとおり、本実施例では最終乾燥水分に到達する迄の時間を比較例1より大幅に短縮できることが明らかになった。また、他の野菜を乾燥する場合にも、上記と同様の傾向が認められた。
【0040】
図2に、実施例及び比較例2の乾燥後のにんじんの組織の模式図(約8倍の組織写真のスケッチ図)を示す。図2(a)は、生鮮状態から直ちに真空凍結乾燥した比較例2の場合で、食品組織1中に数百μmから数mmの空孔2が多数存在している。一方、図2(b)は本実施例の場合で、食品組織1は一様で上記のような大きな空孔は認められない。
【0041】
また、実施例及び比較例1、2の乾燥野菜を水に戻して、その風味を比較したところ、比較例1はやや変質、変色が認められ、比較例2は食感、歯ごたえに変化が認められたのに対して、実施例では変質、変色も少なく、食感、歯ごたえも元の生鮮食品に最も近かった。
【0042】
【発明の効果】
本発明により、非凍結乾燥と真空凍結乾燥を組み合わせて、食品の変質、変色が少なく元の食品の風味を良く残し、長時間保存可能であり、かつ乾燥時間の比較的短い食品の乾燥方法を提供することが可能になった。
【図面の簡単な説明】
【図1】本実施例と比較例におけるにんじんの乾燥速度の比較を示す図。
【図2】本実施例と比較例の乾燥後のにんじんの組織の例を示す模式図。
【図3】常温減圧乾燥法と真空凍結乾燥法における生鮮食品の乾燥速度の比較を示す模式図。
【符号の説明】
1 食品組織
2 空孔
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for drying foods for producing dried foods such as vegetables and seafood, and more particularly, to a drying method for preventing food from being altered or discolored and performing drying.
[0002]
[Prior art]
There are various methods for drying fresh food, such as sun drying, hot air drying, infrared drying, freeze drying, and the like. Recently, a vacuum drying method has attracted attention as a method that can be quickly dried at a relatively low temperature.
[0003]
The reduced-pressure drying method increases the evaporation rate of moisture by reducing the pressure in the drying chamber, and by drying at a temperature close to room temperature, for example, 50 ° C. or less, prevents decomposition of food components, alteration of food, and discoloration. It is an excellent method for obtaining a dry food that retains the flavor of the food.
[0004]
However, even with the vacuum drying method, it takes a considerable amount of time to complete the drying of the food, which causes the propagation of various bacteria and the oxidation of the food components, which are not always sufficient to leave the flavor of the original fresh food. I can't say.
[0005]
Furthermore, there is a vacuum freeze-drying method as another method for drying while leaving the flavor of the original food. This is a drying method in which the object to be dried is cooled to 0 to −40 ° C. and frozen, and then the moisture is removed as a gas in the vacuum drying chamber while being frozen. The pressure in the drying chamber is lower than the vapor pressure of the solid moisture. Therefore, it is necessary to create a high vacuum of, for example, about 50 mm (0.5 kPa) of water column with absolute pressure.
[0006]
In recent years, the vacuum freeze-drying method has been widely used as a method for drying ingredients such as instant foods such as instant noodles, tea pickles, sprinkles, soups, and seasonings. This is to dry the material once boiled, and has the advantage that it can prevent the invasion and propagation of germs in the drying process and is suitable for long-term storage. In addition, it has been attempted to produce fresh foods that can be stored for a long period of time by directly vacuum-freezing and drying fresh foods such as vegetables, meat, and seafood.
[0007]
However, the vacuum freeze-drying method has a very low drying speed, and if all the moisture in the food is removed with this, there is a problem that the drying time becomes extremely long and the drying cost is remarkably increased.
[0008]
[Problems to be solved by the invention]
In view of the problems of the conventional food drying methods as described above, the present invention provides a food drying method that better preserves the flavor of the original food, can be stored for a long time, and has a relatively low drying cost. With the goal.
[0009]
In particular, we provide a food drying method that can achieve both of the two objectives of preventing deterioration of food and reducing the cost of drying by properly combining vacuum drying and other conventional drying methods near room temperature and vacuum freeze drying. The purpose is to do.
[0010]
[Means for Solving the Problems]
The inventors of the present invention examined the drying speed of various fresh foods in conventional drying methods, for example, a method of drying at 40 ° C. or lower under reduced pressure (hereinafter referred to as “room temperature vacuum drying method”) and a vacuum freeze-drying method. It was found that there is a relationship as schematically shown in FIG.
[0011]
That is, the normal temperature reduced pressure drying method has a large initial drying rate, but when the moisture in the food becomes about 20 to 30% of the fresh state, the drying rate starts to decrease, especially when it becomes 15 to 20% or less of the fresh state moisture. Drying almost does not proceed, and it is difficult to reach the final dry moisture (about 3 to 10% of the fresh moisture).
[0012]
On the other hand, in the vacuum freeze-drying method, the initial drying rate is very small, but even if the moisture in the food becomes 20 to 30% or less of the fresh state, the drying rate does not decrease so much and reaches the final dry moisture.
[0013]
The reason for the difference in the drying rate in the low moisture region is considered as follows. That is, in the room temperature vacuum drying method, the drying speed is high at the initial stage of drying because mainly free water in the food tissue (water not bonded to the food tissue) evaporates. On the other hand, in the low moisture region, the water adhering / bonding to the multi-molecular layer mainly evaporates in the food tissue, but this moisture has a large affinity with the food tissue, and therefore the evaporation rate is remarkably slow.
[0014]
In contrast, in the vacuum freeze-drying method, the moisture adhering to and bound to the multi-molecular layer on the food tissue as described above freezes and becomes solid moisture together with free water, and the affinity with the food tissue is almost lost. Is called. This is considered to be the reason why the drying rate does not decrease even in a low moisture region (20 to 30% or less of fresh moisture) in the vacuum freeze-drying method.
[0015]
The inventors of the present invention pay attention to the drying behavior of food as described above, and find that it is possible to perform efficient drying with little alteration of food by appropriately combining non-freeze drying and freeze drying. It was.
[0016]
The present invention has been made on the basis of the above knowledge, and the gist thereof is as follows.
(1) When drying a fresh food or a food prepared by boiling it, it was pre-dried at a temperature of 10 to 40 ° C. until the moisture in the dried product became 10 to 30% of the fresh moisture. Then, it is the drying method of the foodstuff characterized by carrying out vacuum freeze-drying.
[0017]
(2) In addition, the pre-drying, the preceding paragraph and characterized in line Ukoto under a reduced pressure of a water column -30mm~-200mm from atmospheric (1) a method of dry food product according.
[0018]
DETAILED DESCRIPTION OF THE INVENTION
In the present invention, the food to be dried includes, for example, fresh vegetables such as carrots, potatoes, pumpkins, green onions, spinach, fresh seafood such as salmon, salmon, salmon, squid, shrimp, scallops, fresh meat or these Foods boiled and cooked.
[0019]
In the method for drying a food according to the present invention, firstly, the material to be dried is preliminarily dried at a temperature at which it does not freeze, that is, a temperature of 0 ° C. or higher, and then vacuum freeze-dried. It is characterized by being in the range of 10 to 30% of moisture.
[0020]
Hereinafter, the reason for limiting the moisture after preliminary drying to this range will be described.
When vacuum freeze-drying is performed in a state where the moisture of the material to be dried is higher than 30% of the fresh moisture, ice pieces of several hundred μm to several mm are formed in the tissue of the food. Since the voids remain after the ice pieces have evaporated, even if the dried food with such voids is returned to the water, the original fresh texture and chewy texture cannot be obtained, resulting in a food flavor. It drops significantly.
[0021]
The present inventors have found that in any food, there is almost no decrease in flavor due to the formation of such pores when vacuum freeze-dried from 30% or less of fresh water. Therefore, in this invention, the water | moisture content in to-be-dried material after preliminary drying shall be 30% or less of the water | moisture content of a fresh state.
[0022]
Further, according to the knowledge of the present inventors, in the preliminary drying (drying in a non-frozen state), the drying rate starts to decrease at a moisture content of 20 to 30% or less of the fresh state, and the fresh state When the water content is close to 10%, the drying rate is remarkably reduced.
[0023]
For this reason, predrying until the moisture in the material to be dried is lower than 10% of the fresh state is not preferable because the drying time becomes excessive and the quality of the food may change due to propagation of various bacteria. Therefore, in this invention, the water | moisture content in to-be-dried material after preliminary drying shall be 10% or more of the water | moisture content of a fresh state. In addition, from the viewpoint of more completely preventing the quality of the food from being changed, it is preferable to keep the moisture in the material to be dried after preliminary drying at a higher value, for example, 15% or more of the moisture in the fresh state.
[0024]
The method of decreasing the drying rate in the low moisture region in the preliminary drying (drying in a non-freezing state) differs depending on the type of food. Therefore, by measuring the speed of pre-drying and vacuum freeze-drying for each food, the former grasps in advance the moisture value in the material to be dried, which is slower than the latter, and from pre-drying to vacuum freeze-drying around this moisture value. If it moves, the whole drying time can be shortened most.
[0025]
In the present invention, it is based on the results of the present inventors that the moisture that shifts from pre-drying to vacuum freeze-drying is determined based on the moisture in the fresh state. This is because it has been found that the moisture value at which the drying rate is reduced and the formation of pores in the food tissue due to ice pieces can be displayed based on the fresh moisture.
[0026]
In addition, the fresh state here is a state in which agricultural products, marine products, etc. are collected and can be traded on the market as fresh products. Usually, vegetables are about 80 to 95% by weight, and seafood is about 60 to 80% by weight. Contains moisture.
[0027]
In the present invention according to the first aspect, the pre-drying condition may be that the temperature of the material to be dried is 10 to 40 ° C. , and the drying method is not particularly limited. Sun drying, cold-air drying, can be applied a variety of methods such as infrared heating drying, the pressure of the atmosphere during drying may also be a reduced pressure at atmospheric pressure.
[0028]
Further, the method and conditions for vacuum freeze-drying are not particularly limited, and a normal method, for example, a material to be dried is frozen at 0 to −40 ° C. and then a freezing vacuum chamber (absolute pressure is, for example, 50 mm or less water column). What is necessary is just to use the method of enclosing in and drying for a predetermined time.
[0029]
In the present invention according to claim 2, after pre-drying from atmospheric pressure under a reduced pressure of -30 mm to -200 mm of water, the moisture of the material to be dried becomes 10 to 30% of the moisture in the fresh state, followed by vacuum freezing. It is characterized by drying.
[0030]
The reason for performing preliminary drying under reduced pressure is to increase the drying rate at room temperature or a temperature close to this. In this case, the higher the degree of vacuum, the higher the drying speed, but on the other hand, the drying equipment becomes expensive and is not preferable. According to the drying system that supplies air to the drying chamber and exhausts the air with high humidity at the same time as shown in the following embodiments, the drying chamber is slightly depressurized, for example, at a reduced pressure of about -30 mm to -200 mm. The drying speed can be increased sufficiently.
[0031]
In the preliminary drying according to the second aspect of the present invention, it is preferable to install a heating means such as an infrared heater and a temperature measuring means such as a radiant heat temperature sensor in the drying chamber. By adopting such a configuration, the temperature of the object to be dried can be reliably controlled to 10 to 40 ° C. to perform preliminary drying.
[0032]
In the invention of claim 2, the upper limit of the temperature of the material to be dried during the pre-drying is set to 40 ° C. If the temperature is higher than this, it is difficult to avoid deterioration of the food or decomposition of useful components due to the action of enzymes in the food. Because. The lower limit of the temperature of the object to be dried is set to 10 ° C. because the drying speed is too slow even under a reduced pressure, and efficient drying becomes difficult.
[0033]
It is also possible to kill germs and the like by installing an ultraviolet irradiation device in the drying chamber and irradiating the material to be dried for a predetermined time or periodically. Also in the present invention of claim 2, the vacuum freeze-drying conditions and method are not particularly limited, and a normal method may be used.
[0034]
In the present invention, when the moisture content of the material to be dried reaches 10 to 30% of the fresh state, the preliminary drying is finished and the process is shifted to the vacuum freeze-drying. Measure the relationship between the drying time and moisture in the material to be dried under the specified drying conditions, and (2) measure the weight of the material to be dried continuously or periodically during drying. It is possible to use various methods such as a method of judging and transferring a moisture change from weight loss.
[0035]
【Example】
A method for drying foods of the present invention was carried out, in which fresh vegetables such as carrots, pumpkins and yamato potatoes were pre-dried under reduced pressure in a drying chamber having a supply / exhaust means and an infrared heater and then freeze-dried.
[0036]
In the example, the moisture in the material to be dried is preliminarily dried to about 20% of the fresh state, and then vacuum freeze-dried.
[0037]
In the preliminary drying, the temperature of the material to be dried was 40 ° C., the atmospheric pressure in the drying chamber was reduced to a water column of −50 mm, and preliminary drying was performed for about 10 hours. Thereafter, the material to be dried was frozen at −15 to 20 ° C., and freeze-dried in a vacuum tank below the freezing point under a vacuum of an absolute pressure of 0.1 kPa or less for about 15 hours. The final dry moisture was 3-5% of fresh state.
[0038]
On the other hand, Comparative Example 1 was a case where the final dry moisture was dried at a temperature not frozen under reduced pressure, and was dried for about 40 hours under the same conditions as the above preliminary drying. In Comparative Example 2, vacuum lyophilization was performed immediately from the fresh state, and vacuum lyophilization was performed for about 60 hours under the same conditions as described above. In Comparative Example 2, the final dry moisture was not reached within the above time.
[0039]
In FIG. 1, the relationship between the drying time and the water | moisture content in a foodstuff in the Example at the time of drying a carrot and the comparative examples 1 and 2 is shown. As can be seen from the figure, in this example, it was found that the time required to reach the final dry moisture can be significantly reduced as compared with Comparative Example 1. Moreover, when drying other vegetables, the same tendency as the above was recognized.
[0040]
FIG. 2 shows a schematic diagram of the carrot tissue after drying in Example and Comparative Example 2 (a sketch of a structure photograph of about 8 times). FIG. 2A shows the case of Comparative Example 2 that was immediately freeze-dried from the fresh state, and there are a large number of pores 2 of several hundred μm to several mm in the food tissue 1. On the other hand, FIG. 2 (b) shows the case of this example, where the food structure 1 is uniform and no large voids as described above are observed.
[0041]
Moreover, when the dried vegetables of Examples and Comparative Examples 1 and 2 were returned to water and their flavors were compared, Comparative Example 1 showed slight alteration and discoloration, and Comparative Example 2 showed changes in texture and texture. On the other hand, in the Examples, there was little alteration and discoloration, and the texture and crunch were closest to the original fresh food.
[0042]
【The invention's effect】
According to the present invention, there is provided a method for drying a food that combines non-freeze drying and vacuum freeze drying to leave the original food flavor with little alteration and discoloration of the food, can be stored for a long time, and has a relatively short drying time. It became possible to provide.
[Brief description of the drawings]
FIG. 1 is a view showing a comparison of carrot drying rates in the present example and a comparative example.
FIG. 2 is a schematic view showing an example of carrot tissues after drying in Examples and Comparative Examples.
FIG. 3 is a schematic diagram showing a comparison of the drying speed of fresh food between a room temperature vacuum drying method and a vacuum freeze drying method.
[Explanation of symbols]
1 Food organization 2

Claims (2)

生鮮食品又はこれを煮沸調理した食品を乾燥するに際して、被乾燥物中の水分が生鮮状態の水分の10〜30%になるまで被乾燥物を10〜40℃で予備乾燥した後、真空凍結乾燥することを特徴とする食品の乾燥方法。When drying a fresh food or a food prepared by boiling it, the dried product is pre-dried at 10 to 40 ° C. until the moisture in the dried product becomes 10 to 30% of the fresh moisture, and then vacuum freeze-dried. A method for drying a food, characterized by comprising: 前記予備乾燥を、大気圧から水柱−30mm〜−200mmの減圧下で行うことを特徴とする請求項1記載の食品の乾燥方法。The preliminary drying, the drying method of a food according to claim 1, wherein the row Ukoto under a reduced pressure of a water column -30mm~-200mm from atmospheric pressure.
JP28629796A 1996-10-29 1996-10-29 How to dry food Expired - Fee Related JP3653354B2 (en)

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JP2002171950A (en) * 2000-12-11 2002-06-18 Pigeon Corp Dry food material with heat history under pressure and method for producing the same
JP4624432B2 (en) * 2008-01-21 2011-02-02 キム,ジュ−イル Shiitake lyophilization method
CN103411390B (en) * 2013-07-18 2015-09-02 上海海洋大学 A kind of ice temperature Minton dryer and the vacuum drying method of fresh fish fillet ice temperature
KR102164114B1 (en) * 2018-11-19 2020-10-13 농업회사법인 더불어실버팜 주식회사 Method of Manufacturing of Sunsik for Green Kernel Black Bean Using Boil Cooking and Freeze Drying Method

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