JPH07289173A - Method for concentrating, cooking and sterilizing food - Google Patents
Method for concentrating, cooking and sterilizing foodInfo
- Publication number
- JPH07289173A JPH07289173A JP6114002A JP11400294A JPH07289173A JP H07289173 A JPH07289173 A JP H07289173A JP 6114002 A JP6114002 A JP 6114002A JP 11400294 A JP11400294 A JP 11400294A JP H07289173 A JPH07289173 A JP H07289173A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- food
- sterilization
- food material
- boiling
- 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.)
- Pending
Links
Landscapes
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
- General Preparation And Processing Of Foods (AREA)
- Jellies, Jams, And Syrups (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は食品原料を減圧下で加熱
して濃縮調理及び殺菌を行う食品の濃縮調理及び殺菌方
法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for concentrated cooking and sterilization of foods in which food materials are heated under reduced pressure for concentrated cooking and sterilization.
【0002】[0002]
【従来の技術】従来、食品の濃縮調理方法としては、加
熱蒸発法、真空蒸発法、凍結乾燥法、逆浸透膜による方
法等があり、濃縮された食品の例としてはジャム、濃縮
ジュース、ペースト等が知られている。従来の濃縮食品
の製造方法をジャムを例にとって以下に説明する。2. Description of the Related Art Conventionally, as a concentrated cooking method for foods, there are a heating evaporation method, a vacuum evaporation method, a freeze-drying method, a method using a reverse osmosis membrane, etc. Examples of concentrated foods include jam, concentrated juice and paste. Etc. are known. A conventional method for producing a concentrated food product will be described below by taking a jam as an example.
【0003】ジャムを製造するには、まず果実、砂糖、
ペクチン等の食品原料を容器に入れ、その容器を外部か
らガス、熱媒、プレートヒータ等によって加熱すること
によって容器内の食品原料を加熱しながら混合し、更
に、常圧下で加熱を続けて濃縮し、その後、出来上がっ
たものを瓶又は缶などの容器に充填し、キャップで密封
し、更に温湯による殺菌を経た後冷却を行うという工程
を採っている。しかし、かかる従来方法では、加熱、濃
縮の際に、食品原料が100°C近くの沸騰温度に加
熱、維持される為、得られたジャムは本来の果実に比べ
て色調が黒ずんだものとなり、また、香味も減少し、熱
によるビタミンC等の損失も多いという問題点があっ
た。To make jam, first of all, fruit, sugar,
Put food ingredients such as pectin in a container, heat the container from the outside with a gas, heat medium, plate heater, etc. to mix the food ingredients in the container while heating, and then continue heating under normal pressure to concentrate. After that, the process of filling the finished product in a container such as a bottle or a can, sealing with a cap, sterilizing with hot water, and then cooling. However, in such a conventional method, during heating and concentration, the food material is heated and maintained at a boiling temperature near 100 ° C, and thus the obtained jam has a darker color tone than the original fruit, Further, there is a problem that the flavor is reduced and the loss of vitamin C and the like due to heat is large.
【0004】そこで、このような問題点を改善すべく、
食品原料を減圧下で加熱、濃縮する方法が知られてい
る。この方法は、食品原料を減圧下で加熱することによ
って、100°Cよりも低い温度で沸騰を生じさせ、上
述のような熱による果実の劣化を減少させることができ
るものである。Therefore, in order to improve such problems,
A method of heating and concentrating a food material under reduced pressure is known. In this method, by heating the food material under reduced pressure, boiling is caused at a temperature lower than 100 ° C., and the deterioration of fruits due to the heat as described above can be reduced.
【0005】[0005]
【発明が解決しようとする課題】ところが、従来方法で
は、容器内の食品原料の加熱にガス、プレートヒータ等
の外部加熱を用いているため、次のような問題点があっ
た。すなわち、外部加熱のため、食品原料を入れた容器
壁面から食品原料に対して熱が伝達されるが、食品原料
の加熱、濃縮につれて、粘度が徐々に高くなって対流が
生じにくくなり、伝熱が悪くなる。このため、敏速に加
熱を行うには、容器壁面温度を食品原料の沸騰温度より
もかなり高くする必要があるが、その場合、食品原料の
粘度が高く流動しにくいため、沸騰状態といえども場所
による温度の高低差がかなり生じてしまい、一部では過
熱が起こり、容器内壁に焦げつきを生じたり、食品の劣
化を生じたりするという問題があった。これを避けるべ
く、入熱を下げて容器壁面温度を下げると、伝熱のため
の時間が長くなり、風味、鮮度等の低下は改善されず、
また、食品原料中に低温部が生じるため、その低温部で
は殺菌不十分になる等の問題があった。However, the conventional method has the following problems because it uses the external heating such as gas or plate heater to heat the food material in the container. That is, heat is transferred to the food material from the wall surface of the container containing the food material due to external heating, but as the food material is heated and concentrated, the viscosity gradually increases and convection becomes less likely to occur, resulting in heat transfer. Becomes worse. Therefore, in order to perform heating rapidly, it is necessary to raise the temperature of the wall surface of the container considerably higher than the boiling temperature of the food material, but in that case, the viscosity of the food material is high and it is difficult to flow, so even in the boiling state There was a problem in that the difference in temperature caused by the temperature was considerably increased, and some parts were overheated to cause charring of the inner wall of the container or deterioration of food. In order to avoid this, if the heat input is lowered to lower the wall surface temperature of the container, the time for heat transfer becomes longer, and the deterioration of flavor, freshness, etc. is not improved,
Further, since a low temperature part is generated in the food material, there is a problem that sterilization is insufficient in the low temperature part.
【0006】本発明は、かかる従来の問題点に鑑みて為
されたもので、加熱、濃縮時間を短縮すると共に温度分
布を小さくすることによって熱による風味、鮮度等の低
下を防止し、且つ必要な殺菌を行うことの可能な食品の
濃縮調理及び殺菌方法を提供することを目的とする。The present invention has been made in view of the above-mentioned conventional problems, and it is necessary to prevent the deterioration of flavor, freshness, etc. due to heat by shortening the heating and concentrating time and reducing the temperature distribution. An object of the present invention is to provide a concentrated cooking and sterilization method of foods that can be sterilized easily.
【0007】[0007]
【課題を解決するための手段】本発明者等はこれらの問
題点を解決すべく検討の結果、減圧沸騰を殺菌の効果が
現れはじめる40°Cから鮮度が喪失しにくい80°C
までの範囲内の温度にて敏速に行うことができれば、食
品劣化を最小限に抑えながら殺菌を行うことができるこ
と、及び、これを実現する手段としてマイクロ波による
内部加熱を用いると、急速で均一な加熱が可能となるこ
とを見出し、本発明を完成した。すなわち、本発明は、
食品原料を、該食品原料の沸騰温度が40〜80°Cの
範囲内となる減圧下におき、その状態で、前記食品原料
にマイクロ波照射を行って該食品原料を内部加熱し、4
0〜80°Cの範囲内の温度での沸騰状態を急速生起さ
せ且つ維持して濃縮及び殺菌を行うことを特徴とする食
品の濃縮調理及び殺菌方法を要旨とする。Means for Solving the Problems As a result of studies to solve these problems, the inventors of the present invention have found that the boiling point under reduced pressure is 40 ° C at which the effect of sterilization begins to appear, and the freshness is not easily lost at 80 ° C.
If it can be carried out promptly at a temperature within the range up to, it is possible to carry out sterilization while minimizing food deterioration, and if internal heating by microwave is used as a means to achieve this, it will be rapid and uniform. The present invention has been completed by finding out that various heating is possible. That is, the present invention is
The food raw material is placed under a reduced pressure such that the boiling temperature of the food raw material is in the range of 40 to 80 ° C., and in that state, microwave irradiation is performed on the food raw material to internally heat the food raw material, and
A summary is a method for concentrated cooking and sterilization of foods, which comprises rapidly producing and maintaining a boiling state at a temperature in the range of 0 to 80 ° C. for concentration and sterilization.
【0008】本発明方法によって製造する食品の例とし
てはジャム、濃縮ジュース、ペースト等を挙げることが
できる。Examples of foods produced by the method of the present invention include jam, concentrated juice, paste and the like.
【0009】本発明に用いるマイクロ波の周波数は91
5MHz、2450MHz等が考えられるが、日本では
2450MHzを用いるのが一般的であり、これを用い
るのが簡便である。The microwave frequency used in the present invention is 91.
Although 5 MHz, 2450 MHz and the like are conceivable, it is common to use 2450 MHz in Japan, and it is convenient to use this.
【0010】[0010]
【作用】上記した本発明方法では、マイクロ波によって
食品原料中の水分が内部加熱されることにより食品原料
へのほぼ均一な急速入熱が可能であり、加えて減圧の併
用により40〜80°Cの範囲内の温度で且つ温度分布
の小さい状態で沸騰状態が急速生起、維持される。この
ため、短時間での濃縮調理が可能であると共に、食品原
料中に80°Cを越える部分がほとんど発生しないの
で、食品の劣化が生じにくく、色調、風味、鮮度等に優
れた食品を得ることができる。また、食品原料中に40
°Cよりも低い部分がほとんど発生せず、このため殺菌
不良を生じるということもない。In the above-mentioned method of the present invention, the moisture in the food material is internally heated by the microwave so that a uniform and rapid heat input to the food material is possible. A boiling state is rapidly generated and maintained at a temperature within the range of C and a small temperature distribution. For this reason, concentrated cooking can be performed in a short time, and almost no part exceeding 80 ° C is generated in the raw material of the food, so that deterioration of the food hardly occurs and a food excellent in color tone, flavor, freshness, etc. is obtained. be able to. In addition, 40 in food ingredients
Almost no part lower than ° C is generated, so that sterilization failure does not occur.
【0011】本発明方法は上記したように、食品原料を
減圧下におくことによって食品原料を40〜80°Cの
範囲内の温度で沸騰状態とし、その沸騰温度で濃縮及び
殺菌処理するものであるが、その具体的な実施に当たっ
ては、通常、次の二つの方法を採ることが好ましい。 処理期間中、食品原料の処理温度(沸騰温度)を一
定とする方法。 処理期間中、食品原料の処理温度(沸騰温度)を適
当なタイムスケジュールで変更する方法。 ここで、これらの処理温度(沸騰温度)は食品原料に作
用させる圧力によって定まるので、本発明方法の実施に
際しては、所望の処理温度が得られるよう食品原料に作
用させる圧力(減圧)を設定し且つ制御することとな
る。As described above, the method of the present invention is to bring the food material into a boiling state at a temperature within the range of 40 to 80 ° C. by subjecting the food material to a reduced pressure, and to condense and sterilize the food material at the boiling temperature. However, it is usually preferable to adopt the following two methods for the specific implementation. A method in which the processing temperature (boiling temperature) of food ingredients is kept constant during the processing period. A method of changing the processing temperature (boiling temperature) of food ingredients during the processing period with an appropriate time schedule. Here, these treatment temperatures (boiling temperature) are determined by the pressure applied to the food material, so when carrying out the method of the present invention, the pressure applied to the food material (reduced pressure) is set so as to obtain the desired treatment temperature. And it will be controlled.
【0012】以下、この食品原料の処理温度(沸騰温
度)の設定及び圧力設定について説明する。一般に食品
原料の濃縮には低温で行う方が色調、香味等の点で望ま
しいので、この点からは処理温度(沸騰温度)が低温に
なる圧力に設定するのが好ましい。しかし、食品品質の
或る特性は高温の方が望ましい場合もある。例えばイチ
ゴジャムの製造の場合であると、55Torrの圧力を
作用させ、その沸点である40°Cの処理温度で処理し
たものは、本来の果実に近いものとなり、色、香り等に
新鮮なジャムが製造できるが、反面イチゴの持つ青臭さ
は残ったものとなる。それに対して、355Torrの
圧力を作用させ、その沸点である80°Cの処理温度で
処理したものは青臭さは消えるものの、色、香りが減少
するという具合に、出来上がる食品は処理温度に応じた
特徴が現れる。また、殺菌に関しては高温の方が望まし
く、この点からは処理温度(沸騰温度)が高温になる圧
力に設定するのが好ましい。このように、処理温度(沸
騰温度)は食品品質及び殺菌効果に大きく影響している
ので、処理温度の設定に当たってはこれらを考慮して定
めることとなる。Hereinafter, the setting of the processing temperature (boiling temperature) and the pressure setting of the food material will be described. Generally, it is preferable to concentrate the food material at a low temperature in terms of color tone, flavor and the like. From this point, it is preferable to set the pressure at which the processing temperature (boiling temperature) becomes low. However, certain characteristics of food quality may be desirable at higher temperatures. For example, in the case of producing strawberry jam, the one treated with a pressure of 55 Torr and treated at a treatment temperature of 40 ° C, which is the boiling point of the strawberry jam, is close to the original fruit and has a fresh color and aroma. Can be produced, but the odor of strawberries remains. On the other hand, a product treated with a pressure of 355 Torr and treated at a treatment temperature of 80 ° C, which is the boiling point of the food, has a blue odor but disappears in color and aroma. The feature appears. Further, for sterilization, a higher temperature is preferable, and from this point, it is preferable to set a pressure at which the treatment temperature (boiling temperature) becomes high. As described above, the treatment temperature (boiling temperature) has a great influence on the food quality and the sterilization effect, and therefore, the treatment temperature should be set in consideration of these factors.
【0013】例えば、処理期間中、食品原料の処理温度
(沸騰温度)を一定として処理する場合には、目的とす
る食品に要求される特性を考慮して、40〜80°Cの
範囲内で一つの処理温度を設定し、それに応じて食品原
料に作用させる圧力を設定する。そして、この設定圧力
を食品原料に作用させ且つその設定圧力に維持しなが
ら、その食品原料をマイクロ波照射によって内部加熱す
ることにより、沸騰状態が敏速に生起し且つ維持され、
食品原料は所定の処理温度で沸騰状態となり、濃縮及び
殺菌処理が行われる。このように処理温度(沸騰温度)
を一定として処理する場合には、処理期間中食品原料に
作用させる圧力を一定に保っておけばよいので、実施が
容易であり、且つ処理温度が常時一定であるので品質が
安定するという利点が得られる。For example, in the case where the food material is treated at a constant treatment temperature (boiling temperature) during the treatment period, it should be within the range of 40 to 80 ° C in consideration of the characteristics required for the intended food. One processing temperature is set and the pressure applied to the food material is set accordingly. Then, while operating this set pressure on the food material and maintaining it at the set pressure, by internally heating the food material by microwave irradiation, a boiling state is rapidly caused and maintained,
The food material is brought to a boiling state at a predetermined processing temperature, and concentrated and sterilized. In this way the processing temperature (boiling temperature)
In the case of treating with constant, it is sufficient to keep the pressure applied to the food material constant during the treatment period, so that it is easy to carry out, and since the treatment temperature is always constant, there is an advantage that the quality is stable. can get.
【0014】食品原料の処理温度(沸騰温度)を適当な
タイムスケジュールで変更する場合にも、目的とする食
品に要求される特性を考慮して処理温度を定めるが、こ
の場合には更に、各処理温度における処理目的(例え
ば、主として濃縮を目的とするとか、殺菌を目的とする
等)を考慮して処理温度及び期間を設定する。例えば、
食品原料の処理期間を、主として濃縮処理を行う期間
と、主として殺菌処理を行う期間とに分け、それぞれに
好ましい処理温度及び期間を定めることができる。この
場合、食品原料の沸騰温度を、40〜80°Cの範囲内
の第一の温度に保って所望の濃縮を行い、その後、前記
食品原料の沸騰温度を、前記第一の温度よりも高い第二
の温度に変更し、短時間で所望の殺菌を行うという2段
スケジュールとすることが好ましい。このような2段ス
ケジュールを採用すると、濃縮処理に30分程度の長い
時間が必要であっても、濃縮処理を行う第一の温度を比
較的低温に設定することで、食品の風味、鮮度等の低下
を防止することができ、また、殺菌処理を行う第二の温
度を高温とすることで短時間でも十分な殺菌を行うこと
ができ、その間に食品の風味、鮮度等の低下がほとんど
生じない。従って、食品の劣化を防止しながら、必要な
濃縮を行い且つ良好な殺菌を行うことができる。2段ス
ケジールの具体例としては、例えば、40°C×30分
+80°C×2分という2段スケジュールを挙げること
ができる。この場合には、最初の30分で風味等鮮度の
損なわれない形で必要な濃縮がほぼ完了し、後の2分で
ほぼ十分な殺菌が行える。マイクロ波によれば内部に亘
る均一な加熱が行えるため、殺菌に有利な80°Cに急
速昇温させることができ、2分という短時間でも80°
C殺菌の効果を得ることができる。なお、主として濃縮
処理を行う期間を更に分けて、異なる処理温度で濃縮処
理を行う構成としてもよいことは言うまでもない。Even when the processing temperature (boiling temperature) of the food material is changed according to an appropriate time schedule, the processing temperature is determined in consideration of the characteristics required for the intended food. The treatment temperature and the period are set in consideration of the treatment purpose at the treatment temperature (for example, mainly for the purpose of concentration or for the purpose of sterilization). For example,
The processing period of the food material can be divided into a period of mainly performing a concentration process and a period of mainly performing a sterilization process, and a preferable processing temperature and period can be set for each. In this case, the boiling temperature of the food material is maintained at a first temperature in the range of 40 to 80 ° C to perform the desired concentration, and then the boiling temperature of the food material is higher than the first temperature. It is preferable to use a two-stage schedule in which the temperature is changed to the second temperature and desired sterilization is performed in a short time. If such a two-stage schedule is adopted, even if a long time of about 30 minutes is required for the concentration process, by setting the first temperature at which the concentration process is performed to a relatively low temperature, the flavor, freshness, etc. of food can be reduced. It is possible to prevent the deterioration of food, and it is possible to carry out sufficient sterilization even in a short time by setting the second temperature for carrying out the sterilization treatment to a high temperature. Absent. Therefore, it is possible to perform necessary concentration and good sterilization while preventing deterioration of food. Specific examples of the two-stage schedule include a two-stage schedule of 40 ° C. × 30 minutes + 80 ° C. × 2 minutes. In this case, the necessary concentration is almost completed in the first 30 minutes without impairing the freshness such as flavor, and the sufficient sterilization can be performed in the second 2 minutes. Since microwaves can perform uniform heating throughout the interior, the temperature can be rapidly raised to 80 ° C, which is advantageous for sterilization, and 80 ° C even in a short time of 2 minutes.
The effect of C sterilization can be obtained. Needless to say, it is also possible to further divide the period during which the concentration process is mainly performed and perform the concentration process at different process temperatures.
【0015】本発明方法は、又、従来の加熱濃縮調理手
段と併用してもよい。たとえば、外部加熱による真空濃
縮調理を低処理温度(例えば40°C近傍)で行い、或
る程度の濃縮を行った後、その食品原料を本発明方法に
より減圧下で高処理温度(例えば80°C近傍)のマイ
クロ波加熱を短時間行って、最終的な濃縮及び殺菌を行
うことにより、食品の劣化をあまり生じることなく高度
の殺菌レベルが得られる。The method of the present invention may also be used in combination with conventional heat-concentration cooking means. For example, vacuum concentration cooking by external heating is performed at a low treatment temperature (for example, around 40 ° C.), and after a certain degree of concentration, the food material is subjected to a high treatment temperature (for example, 80 ° C.) under reduced pressure by the method of the present invention. By performing microwave heating (near C) for a short time to perform final concentration and sterilization, a high sterilization level can be obtained without causing much deterioration of food.
【0016】本発明方法の実施に当たっては、食品原料
を均一に加熱、昇温させることが必要であるが、そのた
めにはマイクロ波工学所定の工夫を採用して、減圧状態
で食品原料に均一にマイクロ波が照射されるようにすれ
ばよい。また、食品原料の深さはマイクロ波がほぼ均等
に吸収されるような深さとする。食品原料を入れる容器
としては、突沸を考慮して球形のフラスコ状の容器を用
いるなどの工夫を行うのもよい。容器の材質もマイクロ
波を用いる為、できる限り誘電損失の少ない材料を用い
る方が良く、たとえば、ガラス類、ポリエチレン、ポリ
プロピレン等のポリオレフィン類、フッ素樹脂、シリコ
ン樹脂等を用いるのがよい。In carrying out the method of the present invention, it is necessary to uniformly heat and raise the temperature of the food raw material. For that purpose, a certain technique of microwave engineering is adopted to make the food raw material even under reduced pressure. The microwave may be applied. The depth of the food material is such that microwaves are absorbed almost evenly. A container such as a spherical flask-shaped container may be used in consideration of bumping as a container for the food material. Since microwaves are also used as the material of the container, it is preferable to use a material with as little dielectric loss as possible, for example, glass, polyolefins such as polyethylene and polypropylene, fluororesins, and silicone resins.
【0017】[0017]
〔実施例1〕本発明方法を実施するための装置として図
1に示す装置を準備した。すなわち、図1において、1
は減圧室であり、真空ポンプ2により減圧状態に吸引さ
れ、且つマイクロ波発振器3で発生したマイクロ波が導
波管4を通って内部に照射される構成となっている。ま
た、減圧室1内を所望の減圧状態に維持するため、減圧
室1内の圧力を検出する圧力センサ5、電磁弁6を備え
た通気管7及び前記圧力センサ5からの信号に応じて電
磁弁6を開閉する制御装置(図示せず)が設けられてい
る。更に、この減圧室1内において調理と同時に殺菌を
行うため、減圧室内は除菌する必要があり、更に減圧時
から常圧に戻す工程の際、大気中の雑菌を取り込まない
ように、通気管7には除菌の為のフィルタ8を取り付け
ている。なお、9は減圧室1にセットされた平底のフラ
スコ状容器、10はその中に入れられた調理すべき食品
原料である。Example 1 The apparatus shown in FIG. 1 was prepared as an apparatus for carrying out the method of the present invention. That is, in FIG.
Is a decompression chamber, and is configured to be sucked in a decompressed state by the vacuum pump 2 and to be internally radiated with microwaves generated by the microwave oscillator 3 through the waveguide 4. Further, in order to maintain the inside of the decompression chamber 1 at a desired decompression state, a pressure sensor 5 for detecting the pressure inside the decompression chamber 1, a ventilation pipe 7 provided with a solenoid valve 6, and an electromagnetic wave in response to a signal from the pressure sensor 5 are used. A control device (not shown) for opening and closing the valve 6 is provided. Furthermore, since sterilization is performed at the same time as cooking in the decompression chamber 1, it is necessary to sterilize the decompression chamber, and in the process of returning to normal pressure from the time of depressurization, a vent pipe is provided so as not to take in various bacteria in the atmosphere. A filter 8 for removing bacteria is attached to 7. In addition, 9 is a flat-bottomed flask-shaped container set in the decompression chamber 1, and 10 is a food material to be cooked contained therein.
【0018】容量が1リットルのフラスコ状容器9内に
食品原料10として、イチゴ500:砂糖250:ペク
チン1:クエン酸1の割合で混合した原料150gを入
れ、減圧室1内にセットした。次いで、真空ポンプ2に
よって、減圧室1内の圧力を、原料が40°Cで沸騰す
る圧力である55Torrに減圧、維持した状態で、マ
イクロ波出力300Wで30分間マイクロ波照射を行
い、食品原料10を約40°Cで減圧沸騰させ、濃縮調
理し、イチゴジャム107gを得た。As a food material 10, 150 g of a mixed material of strawberry 500: sugar 250: pectin 1: citric acid 1 was placed in a flask-shaped container 9 having a capacity of 1 liter and set in the decompression chamber 1. Then, with the vacuum pump 2, the pressure in the decompression chamber 1 was reduced to 55 Torr, which is the pressure at which the raw material boils at 40 ° C., and was maintained at a microwave output of 300 W for 30 minutes to perform microwave irradiation. 10 was boiled under reduced pressure at about 40 ° C. and concentrated and cooked to obtain 107 g of strawberry jam.
【0019】〔比較例1〕実施例1と同原料150gを
用い、加熱のためにフラスコ状容器9の底面にプレート
ヒータを配置し、実施例1と同減圧条件にて、プレート
ヒータ出力300Wで加熱し、加熱時間30分にてイチ
ゴジャム133gを得た。実施例1と比較例1のそれぞ
れによって得たイチゴジャムを、20名パネルにより官
能評価した。その結果を表1に示す。Comparative Example 1 150 g of the same raw material as in Example 1 was used, a plate heater was placed on the bottom surface of the flask-like container 9 for heating, and the plate heater output was 300 W under the same reduced pressure conditions as in Example 1. The mixture was heated and heating time was 30 minutes to obtain 133 g of strawberry jam. The strawberry jam obtained in each of Example 1 and Comparative Example 1 was sensory-evaluated by a panel of 20 people. The results are shown in Table 1.
【0020】[0020]
【表1】 [Table 1]
【0021】表1から明らかなように、比較例1では濃
縮調理が不十分で、且つ風味が低下しているが、実施例
1ではこれらが著しく改善された。As is apparent from Table 1, in Comparative Example 1, the concentrated cooking was insufficient and the flavor was deteriorated, but in Example 1, these were remarkably improved.
【0022】〔実施例2〕実施例1と同装置、同原料に
て、減圧室1内の圧力をそれぞれ、 55Torr(減圧沸騰温度40°C) 92.5Torr(減圧沸騰温度50°C) 150Torr(減圧沸騰温度60°C) に設定し、マイクロ波加熱出力300W、マイクロ波照
射時間30分にてジャムを製造した。処理後のジャムを
無菌的に取り出し、無菌室へ持ち込み、蒸発水分量の補
正を行った後、各1gを殺菌済シャーレに分取した。殺
菌済培養寒天を10cc流し込んで培地を作り、インキ
ュベータにて30°C、48時間培養を行い、菌数を計
測した。その結果を表2に示す。[Embodiment 2] Using the same apparatus and the same raw material as in Embodiment 1, the pressure in the decompression chamber 1 was 55 Torr (reduced pressure boiling temperature 40 ° C.) 92.5 Torr (reduced pressure boiling temperature 50 ° C.) 150 Torr (Depressurized boiling temperature 60 ° C) was set, and a jam was produced at a microwave heating output of 300 W and a microwave irradiation time of 30 minutes. The treated jam was aseptically taken out, brought into a sterile room, the amount of evaporated water was corrected, and 1 g of each was dispensed into a sterilized petri dish. 10 cc of sterilized culture agar was poured into the medium to make a medium, and the medium was cultured at 30 ° C. for 48 hours in an incubator to count the number of bacteria. The results are shown in Table 2.
【0023】〔比較例2〕同様にプレートヒータを用
い、実施例2に対応する条件で同数のジャムを製造し
た。得られたジャムを用いて実施例2と同様に無菌操作
にて培養を行い、菌数を計測した。同時に対照して加熱
処理前の原料を培養し、菌数を計測した。その結果を表
2に示す。[Comparative Example 2] The same number of jams were manufactured under the conditions corresponding to those of Example 2 using the plate heater in the same manner. The obtained jam was cultivated by aseptic operation in the same manner as in Example 2, and the number of bacteria was counted. At the same time, in contrast, the raw material before the heat treatment was cultured and the number of bacteria was counted. The results are shown in Table 2.
【0024】表2から明らかなように、実施例2で得た
ジャムの殺菌状態は、それぞれの温度において対応する
比較例2に比べ改善されていることが判明した。この理
由は、比較例2に比べ実施例2では温度分布が小さくな
り、異常に低温の部分が生じていないためと思われる。As is clear from Table 2, the sterilization state of the jam obtained in Example 2 was found to be improved as compared with the corresponding Comparative Example 2 at each temperature. This is probably because the temperature distribution in Example 2 was smaller than that in Comparative Example 2 and no abnormally low temperature portion was generated.
【0025】[0025]
【表2】 [Table 2]
【0026】〔実施例3〕実施例1と同装置、同原料に
て、表3に示す減圧沸騰温度で且つ表3に示す時間だけ
マイクロ波照射を行い、濃縮調理を行った。また、その
処理の前後における全体重量(フラスコ状容器9を含む
重量)を測定して、減量(水分蒸発量)を測定した。そ
の結果を表3に示す。Example 3 Using the same equipment and the same raw material as in Example 1, microwave irradiation was carried out at the reduced pressure boiling temperature shown in Table 3 and for the time shown in Table 3 to perform concentrated cooking. In addition, the total weight (weight including the flask-shaped container 9) before and after the treatment was measured to measure the weight loss (water evaporation amount). The results are shown in Table 3.
【0027】〔比較例3〕同様にプレートヒータを用
い、表3に示す条件で濃縮調理を行い、その処理前後に
おける全体重量を測定して減量を求めた。その結果も表
3に示す。なお、この時のフラスコ状容器9の底部壁面
温度を測定したので、その結果も示す。[Comparative Example 3] Similarly, a plate heater was used to perform concentrated cooking under the conditions shown in Table 3, and the total weight before and after the treatment was measured to determine the weight loss. The results are also shown in Table 3. The temperature of the bottom wall surface of the flask-shaped container 9 at this time was measured, and the results are also shown.
【0028】実施例3の各々における濃縮調理後のフラ
スコ状容器内の原料を観察したところ、いずれの条件の
ものも何ら異常は見られなかった。一方、比較例3の場
合にはいずれにおいても容器底部に一部固着が見られ
た。これは表3に示したように容器底部が高温になって
いるためと思われる。因に、実施例3においては容器壁
の温度が処理温度より高くなるという現象は見られなか
った。また、表3から明らかなように、比較例3に比べ
て実施例3では、同一温度においても、濃縮速度が早
く、しかも固着がほとんど生じないことが確認された。When the raw materials in the flask-shaped container after the concentrated cooking in each of Example 3 were observed, no abnormality was found under any of the conditions. On the other hand, in the case of Comparative Example 3, in all cases, some sticking was observed at the bottom of the container. This is probably because the bottom of the container is at a high temperature as shown in Table 3. Incidentally, in Example 3, the phenomenon that the temperature of the container wall became higher than the processing temperature was not observed. Further, as is clear from Table 3, it was confirmed that in Example 3, compared with Comparative Example 3, even at the same temperature, the concentration rate was faster and the sticking hardly occurred.
【0029】[0029]
【表3】 [Table 3]
【0030】[0030]
【発明の効果】以上の説明から明らかなように、本発明
は、食品原料をマイクロ波照射することにより、食品原
料を内部加熱し、ほぼ均一な急速入熱が可能であり、し
かもその食品原料が40〜80°Cの範囲内の温度で沸
騰するように減圧しておくことにより、温度分布の小さ
い状態で40〜80°Cの範囲内での沸騰状態に維持す
ることができ、このため、食品の変色や風味、鮮度等の
低下が少なく、短時間で濃縮調理及び殺菌ができるとい
う効果を有している。EFFECTS OF THE INVENTION As is clear from the above description, according to the present invention, by irradiating a food material with microwaves, the food material is internally heated and a substantially uniform rapid heat input is possible. By decompressing so that it boils at a temperature in the range of 40 to 80 ° C, it is possible to maintain the boiling state in the range of 40 to 80 ° C with a small temperature distribution. In addition, there is little discoloration of food, deterioration of flavor, freshness, and the like, and it has an effect that concentrated cooking and sterilization can be performed in a short time.
【0031】ここで、食品原料の沸騰温度を40〜80
°Cの範囲内の一定温度とする場合には、食品原料に作
用させる圧力を一定に維持しておけばよいので、実施が
容易であり、且つ食品品質を均一に保つことができると
いう効果が得られる。また、沸騰温度を40〜80°C
の範囲内の第一の温度に保って所望の濃縮を行い、その
後、前記第一の温度よりも高い第二の温度に変更し、短
時間で所望の殺菌を行うという方法を採用すれば、食品
の変色や風味、鮮度等の低下をあまり生じることなく殺
菌効果を大幅に向上させることができるという効果が得
られる。Here, the boiling temperature of the food material is set to 40-80.
When the temperature is kept constant within the range of ° C, it is sufficient to keep the pressure applied to the food material constant, so that it is easy to carry out and the food quality can be kept uniform. can get. The boiling temperature is 40 to 80 ° C.
The desired concentration is maintained at a first temperature within the range of, and then changed to a second temperature higher than the first temperature, and if a method of performing desired sterilization in a short time is adopted, The effect that the bactericidal effect can be greatly improved can be obtained without causing much discoloration, flavor, freshness, etc. of the food.
【図1】本発明方法の実施に用いる装置の1例を示す概
略断面図FIG. 1 is a schematic sectional view showing an example of an apparatus used for carrying out the method of the present invention.
【符号の説明】 1 減圧室 2 真空ポンプ 3 マイクロ波発振器 4 導波管 5 圧力センサ 6 電磁弁 7 通気管 8 フィルタ 9 フラスコ状容器 10 食品原料[Explanation of symbols] 1 decompression chamber 2 vacuum pump 3 microwave oscillator 4 waveguide 5 pressure sensor 6 solenoid valve 7 ventilation pipe 8 filter 9 flask-shaped container 10 food material
Claims (3)
0〜80°Cの範囲内となる減圧下におき、その状態
で、前記食品原料にマイクロ波照射を行って該食品原料
を内部加熱し、40〜80°Cの範囲内の温度での沸騰
状態を急速生起させ且つ維持して濃縮及び殺菌を行うこ
とを特徴とする食品の濃縮調理及び殺菌方法。1. A food material having a boiling temperature of 4
It is placed under a reduced pressure in the range of 0 to 80 ° C, and in that state, the food material is subjected to microwave irradiation to internally heat the food material, and boiling at a temperature in the range of 40 to 80 ° C. A method for concentrated cooking and sterilization of foods, which comprises rapidly producing and maintaining a state for concentration and sterilization.
°Cの範囲内の一定温度に保って濃縮及び殺菌を行うこ
とを特徴とする請求項1記載の食品の濃縮調理及び殺菌
方法。2. The boiling temperature of the food material is 40 to 80.
2. The method of concentrated cooking and sterilization of food according to claim 1, wherein the concentration and sterilization are carried out while maintaining a constant temperature within a range of ° C.
°Cの範囲内の第一の温度に保って所望の濃縮を行い、
その後、前記食品原料の沸騰温度を、前記第一の温度よ
りも高い第二の温度に変更し、短時間で所望の殺菌を行
うことを特徴とする請求項1記載の食品の濃縮調理及び
殺菌方法。3. The boiling temperature of the food material is 40-80.
Maintain the first temperature in the range of ° C to achieve the desired concentration,
After that, the boiling temperature of the food material is changed to a second temperature higher than the first temperature, and desired sterilization is performed in a short time, concentrated cooking and sterilization of the food according to claim 1. Method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6114002A JPH07289173A (en) | 1994-04-28 | 1994-04-28 | Method for concentrating, cooking and sterilizing food |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6114002A JPH07289173A (en) | 1994-04-28 | 1994-04-28 | Method for concentrating, cooking and sterilizing food |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07289173A true JPH07289173A (en) | 1995-11-07 |
Family
ID=14626606
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6114002A Pending JPH07289173A (en) | 1994-04-28 | 1994-04-28 | Method for concentrating, cooking and sterilizing food |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07289173A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010013583A1 (en) * | 2008-07-30 | 2010-02-04 | 国立大学法人九州工業大学 | Method for producing dry article and apparatus therefor |
-
1994
- 1994-04-28 JP JP6114002A patent/JPH07289173A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010013583A1 (en) * | 2008-07-30 | 2010-02-04 | 国立大学法人九州工業大学 | Method for producing dry article and apparatus therefor |
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