JP2000060511A - Thermal sterilization - Google Patents

Thermal sterilization

Info

Publication number
JP2000060511A
JP2000060511A JP10246540A JP24654098A JP2000060511A JP 2000060511 A JP2000060511 A JP 2000060511A JP 10246540 A JP10246540 A JP 10246540A JP 24654098 A JP24654098 A JP 24654098A JP 2000060511 A JP2000060511 A JP 2000060511A
Authority
JP
Japan
Prior art keywords
superheated steam
pressure
heating chamber
microwave heating
steam
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
Application number
JP10246540A
Other languages
Japanese (ja)
Inventor
Tomio Minobe
富男 美濃部
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.)
Micro Denshi Co Ltd
Original Assignee
Micro Denshi Co Ltd
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 Micro Denshi Co Ltd filed Critical Micro Denshi Co Ltd
Priority to JP10246540A priority Critical patent/JP2000060511A/en
Publication of JP2000060511A publication Critical patent/JP2000060511A/en
Pending legal-status Critical Current

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  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • Apparatus For Disinfection Or Sterilisation (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for thermal sterilization by applying microwaves and superheated steam decompressed to a pressure near to the atmospheric pressure to target articles to sterilize the articles. SOLUTION: This method for thermal sterilization comprises decompressing saturated steam B1 supplied from a boiler 57 and having a pressure of about 5-10 kg/cm2 G to a pressure of about 0.1-0.7 kg/cm2 G by the use of a pressure- reducing valve 59, heating the obtained steam B1 with a heater 60 up to a temperature of about 110-300 deg.C to produce a superheated steam B2, transferring the superheated steam B2 into a microwave heating chamber 50, and subsequently quickly heating target articles A with the superheated steam and microwaves in the microwave heating chamber 50 to sterilize the articles A.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】この発明は、粉粒物食品であ
る被殺菌物にマイクロ波と過熱蒸気とを与えて殺菌する
加熱殺菌方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat sterilization method for sterilizing an object to be sterilized, which is a granular food, by applying microwaves and superheated steam.

【0002】[0002]

【従来の技術】粉粒物食品には、穀物、玄そば、豆類、
香辛料、乾燥野菜、健康食品などがあるが、その種類が
多く、また、その形状、粒度もさまざまで、3〜15%
程度の水分をもっているものが多い。
2. Description of the Related Art Grain, gen buckwheat, beans,
There are spices, dried vegetables, health foods, etc., but there are many types, and their shapes and particle sizes are various, and 3 to 15%.
Many have a certain amount of water.

【0003】このような粉粒物食品は、一般に乾燥、成
熟、粉砕などの処理工程を得て加工されるため、非常に
汚染されている場合がある。例えば、香辛料、玄そばな
どは土壌菌などで極端に汚染され、菌数が105〜108
(個/g)にもなる。
[0003] Since such a granular food is generally processed by obtaining processing steps such as drying, ripening and crushing, it may be extremely contaminated. For example, spices, gen buckwheat, etc. are extremely polluted with soil fungi and the number of bacteria is 10 5 to 10 8
It can also be (pieces / g).

【0004】上記した粉粒物食品の殺菌には、殺菌効果
の高い過熱蒸気を利用した気流式殺菌装置が広く使用さ
れている。
For the sterilization of the above-mentioned powdery or granular food, an air flow type sterilizer utilizing superheated steam having a high sterilizing effect is widely used.

【0005】この気流式殺菌装置は、粉粒物の搬送及び
加熱に蒸気の気流を用いる。具体的には、殺菌の圧力を
1〜3Kg/cm2G、温度を120〜260℃程度に
した過熱蒸気を流速10〜30m/秒の高速でパイプ内
を循環させ、そのパイプ内を粉粒物が浮遊しながら搬
送、加熱される。
This air flow type sterilizer uses a steam air flow for transporting and heating powdery or granular materials. Specifically, superheated steam having a sterilization pressure of 1 to 3 Kg / cm 2 G and a temperature of about 120 to 260 ° C. is circulated in the pipe at a high speed with a flow rate of 10 to 30 m / sec, and the powder in the pipe is granulated. Objects are transported and heated while floating.

【0006】また、プラスチックフイルムを貼り合わせ
たパウジ(袋)や成形容器などに食品を詰めて密封され
ているレトルト食品の加熱殺菌には、レトルト殺菌装置
が使用されている。
Further, a retort sterilizer is used for heat sterilization of retort foods in which foods are packed and sealed in pouches (bags) or molded containers to which plastic films are attached.

【0007】このレトルト殺菌装置は、圧力釜内にレト
ルト食品を入れ、圧力釜内に導入する蒸気や熱水によっ
て、パウジや容器の食品を加熱し、食品の温度を、例え
ば、120℃で3分間保つこにより、食品を加熱殺菌す
る。
This retort sterilizer puts the retort food in a pressure cooker and heats the food in the pauge or the container by steam or hot water introduced into the pressure cooker, and the temperature of the food is, for example, 3 at 120 ° C. Heat sterilize the food by keeping it for a minute.

【0008】[0008]

【発明が解決しようとする課題】上記した気流式殺菌装
置による殺菌方法は、急速な加熱が可能であり、殺菌効
果の高い殺菌方法であると言われている。
The sterilization method using the above-mentioned air flow type sterilization apparatus is said to be a sterilization method capable of rapid heating and having a high sterilization effect.

【0009】しかし、この殺菌方法を実施するには、粉
粒物を加圧系内に供給する手段や粉粒物を蒸気と分離し
て加圧系外に捕集する機構などの圧力シ−ル等が複雑と
なり、殺菌装置が高価なシステム構成となる。また、粉
粒物を気流で搬送する構成であるため、レトルト食品の
ような嵩張った食品については殺菌することができな
い。
However, in order to carry out this sterilization method, a pressure system such as a means for supplying the granular material into the pressurizing system or a mechanism for separating the granular material from the vapor and collecting it outside the pressurizing system is used. However, the sterilizer has an expensive system configuration. Further, since the powdery or granular material is conveyed by the air flow, bulky foods such as retort foods cannot be sterilized.

【0010】上記したレトルト殺菌装置による殺菌方法
は、圧力釜内に導入される蒸気や熱水より、パウジや成
形容器を介して食品の表面より中心へ熱伝達して殺菌す
る方法である。
The sterilization method using the above-mentioned retort sterilization apparatus is a method for sterilizing heat from steam or hot water introduced into the pressure cooker to the center from the surface of the food through the page and the molding container.

【0011】したがつて、例えば、120℃まで昇温す
る時間が40分程度かかるため、食品の表面が高温に長
時間さらされることになり、このことから、食品の味、
香り、食感などの品質が低下すると言う問題がある。
Therefore, for example, it takes about 40 minutes to raise the temperature to 120 ° C., so that the surface of the food is exposed to a high temperature for a long time.
There is a problem that the quality such as aroma and texture deteriorates.

【0012】また、このレトルト殺菌装置による殺菌方
法は、圧力釜による加圧加熱法となるために、粉粒物の
連続殺菌化が難しいことから、粉粒物食品の生産上にお
いて問題となっている。さらに、圧力釜を使用するた
め、安全性の面で保守、点検、管理が大変となる。
Further, since the sterilization method using the retort sterilization apparatus is a pressure heating method using a pressure cooker, continuous sterilization of the powder and granules is difficult, which is a problem in the production of the powder and granular foods. There is. Furthermore, since the pressure cooker is used, maintenance, inspection and management are difficult in terms of safety.

【0013】本発明は、上記した実情にかんがみ、常圧
(大気圧)に近い過熱蒸気とマイクロ波を併用して被殺
菌物を短時間で殺菌する加熱殺菌方法を提案することを
目的とする。
In view of the above-mentioned circumstances, the present invention has an object of proposing a heat sterilization method for sterilizing an object to be sterilized in a short time by using superheated steam near atmospheric pressure (atmospheric pressure) and microwaves together. .

【0014】[0014]

【課題を解決するための手段】上記した目的を達成する
ため、本発明では、マイクロ波加熱室内でマイクロ波エ
ネルギ−と水蒸気エネルギ−とを被殺菌物に与えて殺菌
する加熱殺菌方法に関する。
In order to achieve the above object, the present invention relates to a heat sterilization method in which microwave energy and water vapor energy are applied to an object to be sterilized in a microwave heating chamber.

【0015】そして、この発明では、水蒸気の圧力を大
気圧近くまで減圧すると共に、この水蒸気の温度を11
0〜300℃程度まで昇温してマイクロ波加熱室内を過
熱蒸気の雰囲気状態とし、被殺菌物にマイクロ波と水蒸
気とを与えて加熱殺菌する構成となっている。
In the present invention, the pressure of the steam is reduced to near atmospheric pressure, and the temperature of the steam is set to 11
The temperature is raised to about 0 to 300 ° C. to bring the microwave heating chamber into an atmosphere of superheated steam, and microwaves and steam are applied to the sterilization object for heat sterilization.

【0016】また、この発明は、マイクロ波室内に熱風
を送り、マイクロ波加熱室内の過熱蒸気を保温する構成
としてある。
Further, the present invention has a structure in which hot air is sent into the microwave chamber to keep the superheated steam in the microwave heating chamber warm.

【0017】[0017]

【作用】この発明は温度100〜110℃程度の飽和水
蒸気をほぼ大気圧(常圧)近くまで減圧した状態で、こ
の水蒸気を電気ヒ−タ−、ガスヒ−タ−などの熱源を利
用して110〜300℃まで昇温する。この昇温によっ
てマイクロ波加熱室内が過熱蒸気の雰囲気状態となる。
According to the present invention, saturated steam having a temperature of about 100 to 110 ° C. is depressurized to near atmospheric pressure (normal pressure), and the steam is utilized by a heat source such as an electric heater or a gas heater. The temperature is raised to 110 to 300 ° C. Due to this temperature rise, the inside of the microwave heating chamber is brought into an overheated steam atmosphere.

【0018】これより、マイクロ波加熱室にある被殺菌
物が、水蒸気によって表面から昇温すると同時にマイク
ロ波の照射によって内部が発熱する。この結果、被殺菌
物の内外部から均一に急速加熱して殺菌することができ
る。なお、本発明は人間の食品にかぎらず、動物の食品
についても同様に殺菌することができる。
As a result, the substance to be sterilized in the microwave heating chamber is heated from the surface by the steam, and at the same time, the interior of the microwave heating chamber is heated by the irradiation of microwaves. As a result, the object to be sterilized can be rapidly heated uniformly from inside and outside to sterilize it. It should be noted that the present invention is not limited to human food, and can similarly sterilize animal food.

【0019】また、本発明は、過熱蒸気の温度が飽和温
度以下に降下し、被殺菌物が吸湿したり、また、マイク
ロ波加熱室の内壁面や被殺菌物を出し入れするマイクロ
波加熱室の開口部内壁に水滴が付着することを防ぐた
め、温度調節できる熱風発生機を使ってマイクロ波加熱
室内に熱風を送る手段を採用している。
Further, according to the present invention, the temperature of the superheated steam is lowered to the saturation temperature or lower, the substance to be sterilized absorbs moisture, and the inner wall surface of the microwave heating chamber and the microwave heating chamber for putting in and out the substance to be sterilized. In order to prevent water droplets from adhering to the inner wall of the opening, a means for sending hot air into the microwave heating chamber using a hot air generator with adjustable temperature is adopted.

【0020】[0020]

【発明の実施の形態】次に、本発明の一実施形態につい
て図面に沿って説明する。図1は本発明の加熱殺菌方法
を実施するための加熱殺菌装置を示す機構図である。
BEST MODE FOR CARRYING OUT THE INVENTION Next, an embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a mechanism diagram showing a heat sterilization apparatus for carrying out the heat sterilization method of the present invention.

【0021】この図において、50は断熱構造としたマ
イクロ波加熱室で、この加熱室50の左右側にはマイク
ロ波漏洩防止対策を施したフィルタ−付の開口部51、
52が設けてある。
In the figure, reference numeral 50 designates a microwave heating chamber having a heat insulating structure. On the left and right sides of the heating chamber 50, there are openings 51 with a filter for preventing microwave leakage,
52 is provided.

【0022】また、このマイクロ波加熱室50には、被
殺菌物Aを開口部51から52に向かって移送する搬送
ベルト53が設けてある。なお、この搬送ベルト53は
モ−タ54によって駆動する。
Further, the microwave heating chamber 50 is provided with a conveyor belt 53 for transferring the sterilization object A from the openings 51 to 52. The conveyor belt 53 is driven by the motor 54.

【0023】さらに、マイクロ波加熱室50の開口部5
1、52には過熱蒸気の排気ダクト55、56を接続
し、これら排気ダクト55、56を手動式ダンパ−とし
て排気量を調整する構造となっている。なお、必要に応
じ排気ブロア−に接続して強制排気するようにしてもよ
い。
Further, the opening 5 of the microwave heating chamber 50
Exhaust ducts 55 and 56 for superheated steam are connected to 1 and 52, and the exhaust amount is adjusted by using these exhaust ducts 55 and 56 as manual dampers. If necessary, an exhaust blower may be connected for forced exhaust.

【0024】一方、ボイラ57より送られる5〜10
(Kg/cm2G)程度(ゲ−ジ圧力)の飽和水蒸気B
1は、仕切弁58を経て圧力調整用の減圧弁59によ
り、その圧力を0.1〜0.7(Kg/cm2G)程度
に減圧調整する構成としてある。
On the other hand, 5 to 10 sent from the boiler 57
Saturated water vapor B of about (Kg / cm 2 G) (gauge pressure)
1 has a configuration in which the pressure is reduced to about 0.1 to 0.7 (Kg / cm 2 G) by the pressure reducing valve 59 for pressure adjustment via the gate valve 58.

【0025】さらに、このように減圧された飽和水蒸気
B1は、電気ヒ−タ−やガスヒ−タ−などからなる熱交
換式加熱ヒ−タ−60によって、温度110〜300℃
程度まで昇温させて過熱蒸気B2を生成する。なお、過
熱蒸気B2は、マイクロ波加熱室50と加熱ヒ−タ−6
0とを接続する配管61の一部に設けた温度センサ−6
2の検出信号にしたがって予め設定した温度に調整する
ようにしてある。
Further, the saturated steam B1 thus depressurized is heated at a temperature of 110 to 300 ° C. by a heat exchange type heating heater 60 composed of an electric heater or a gas heater.
The temperature is raised to a certain degree to generate superheated steam B2. The superheated steam B2 is used in the microwave heating chamber 50 and the heating heater-6.
Temperature sensor 6 provided in a part of the pipe 61 for connecting to 0
According to the detection signal of No. 2, the temperature is adjusted to a preset temperature.

【0026】このように生成された過熱蒸気B2は配管
の吹出孔63a、63b、63c・・・・・よりマイク
ロ波加熱室50内に吹き出し、この加熱室50内に充満
する。
The superheated steam B2 thus generated is blown into the microwave heating chamber 50 through the blowout holes 63a, 63b, 63c of the pipes, and the heating chamber 50 is filled with the microwave heating chamber 50.

【0027】他方、マイクロ波加熱室50の底面側に
は、リタ−ンダクトに接続した耐熱用の循環ファン64
と、加熱ヒ−タ65と、吹き出しダクトの一部に設けた
熱風温度センサ−66とによって構成した熱風発生機が
配備してある。
On the other hand, on the bottom side of the microwave heating chamber 50, a heat-resistant circulation fan 64 connected to a return duct.
A hot air generator including a heating heater 65 and a hot air temperature sensor 66 provided in a part of the blowing duct is provided.

【0028】この熱風発生機の循環熱風温度は予め設定
した温度になるように熱風温度センサ−66の検出信号
にしたがってコントロ−ルする。このことから、マイク
ロ波加熱室50内の過熱蒸気がこの熱風発生機の熱風に
よって循環されながら熱が補充され、この過熱蒸気の温
度が保温される。
The circulating hot air temperature of the hot air generator is controlled according to the detection signal of the hot air temperature sensor 66 so as to reach a preset temperature. From this, the superheated steam in the microwave heating chamber 50 is supplemented with heat while being circulated by the hot air of the hot air generator, and the temperature of the superheated steam is kept warm.

【0029】またマイクロ波は、マイクロ波発振機67
より発振され、導波管68の先端の照射口よりマイクロ
波加熱室50内に照射される。なお、マイクロ波の照射
口には、テフロン、セラミック、石英ガラス等の材料を
用いたシ−ル板69を設け、導波管68内への過熱蒸気
の侵入を防ぐようにしてある。
The microwave is generated by the microwave oscillator 67.
The microwave is oscillated and is irradiated into the microwave heating chamber 50 through the irradiation opening at the tip of the waveguide 68. A seal plate 69 made of a material such as Teflon, ceramics, or quartz glass is provided at the microwave irradiation port to prevent the superheated vapor from entering the waveguide 68.

【0030】次に、上記した加熱殺菌装置を用いた殺菌
方法について説明する。先ず、マイクロ波加熱室50に
被殺菌物Aを搬入する前に循環ファン64と加熱ヒ−タ
−65を動作させて熱風発生機を運転し、マイクロ波加
熱室50内やその左右側の開口部51、52の内壁を昇
温させる。
Next, a sterilization method using the above-mentioned heat sterilization apparatus will be described. First, before the object A to be sterilized is carried into the microwave heating chamber 50, the circulating fan 64 and the heating heater 65 are operated to operate the hot air generator, and the openings in the microwave heating chamber 50 and the left and right sides thereof are opened. The inner walls of the parts 51 and 52 are heated.

【0031】これは、マイクロ波加熱室50の内壁や被
殺菌物の温度が低い場合に、過熱蒸気の熱が奪われ、こ
の過熱蒸気の温度が下がることによって発生する水滴を
防止するためである。
This is to prevent water droplets generated by the heat of the superheated steam being taken away when the temperature of the inner wall of the microwave heating chamber 50 or the object to be sterilized is low and the temperature of the superheated steam lowering. .

【0032】続いて、仕切弁58を開いて飽和水蒸気B
1を減圧弁59に送り、この減圧弁59によりこの水蒸
気B1を所定圧力にまで減圧する。このように減圧され
た飽和水蒸気B1が加熱ヒ−タ−60に送られ、この加
熱ヒ−タ−60によって目的の所定温度(110〜30
0℃)に昇温された過熱蒸気B2が配管61より送り出
される。
Then, the sluice valve 58 is opened and saturated water vapor B is added.
1 is sent to the pressure reducing valve 59, and the water vapor B1 is reduced to a predetermined pressure by the pressure reducing valve 59. The saturated steam B1 thus depressurized is sent to the heating heater 60, and the heating heater 60 causes the heating heater 60 to reach a predetermined temperature (110 to 30).
The superheated steam B2 heated to 0 ° C.) is sent out from the pipe 61.

【0033】このように送り出される過熱蒸気B2は、
既に述べたように、0.1〜0.7(Kg/cm2G)
の圧力で、110〜300℃の温度となっており、この
過熱蒸気B2が吹出口63a、63b、63c・・・・
・よりマイクロ波加熱室50内に放出される。
The superheated steam B2 thus sent out is
As already mentioned, 0.1-0.7 (Kg / cm 2 G)
At a pressure of 110 to 300 ° C., this superheated steam B2 is blown out by the blowout ports 63a, 63b, 63c ...
-More radiated into the microwave heating chamber 50.

【0034】また、マイクロ波加熱室50に放出された
過熱蒸気が冷たい部所に触れると結露が発生するため、
循環ファン64と加熱ヒ−タ−65を常時運転し、過熱
蒸気の温度を低下させずに、設定過熱温度を保ち続ける
ように熱の補給を行なう。
Further, when the superheated steam discharged into the microwave heating chamber 50 touches a cold part, dew condensation occurs,
The circulation fan 64 and the heating heater 65 are constantly operated to supply heat so as to keep the set superheat temperature without lowering the temperature of the superheated steam.

【0035】このように過熱蒸気の雰囲気状態としたマ
イクロ波加熱室50内に被殺菌物Aを搬送ベルト53に
乗せて開口部51より順次送り込む。これにより、被殺
菌物Aが過熱蒸気により外面から加熱され、また、マイ
クロ波の照射を受けて分子振動を起こし内部から発熱す
ることから、被殺菌物Aの内外が均一に高速加熱殺菌処
理される。
In this manner, the sterilized object A is placed on the conveyor belt 53 in the microwave heating chamber 50 in the superheated steam atmosphere, and is sequentially fed from the opening 51. As a result, the substance A to be sterilized is heated from the outer surface by superheated steam, and molecular vibration is generated by the irradiation of microwaves to generate heat from the inside. Therefore, the inside and outside of the substance A to be sterilized are uniformly heat-sterilized at high speed. It

【0036】なお、殺菌された殺菌物は開口部52から
順次搬送され、その後、必要に応じて冷却工程を経て冷
却される。
The sterilized sterilized product is successively conveyed from the opening 52, and then cooled through a cooling step as needed.

【0037】また、この加熱殺菌装置は、左右の排気ダ
クト55、56によって、マイクロ波加熱室50に供給
される過熱蒸気B2の分量だけ常時排出させる。このこ
とから、過熱蒸気の圧力が若干程度(0.1〜0.7K
g/cm2G程度)存在しても、マイクロ波加熱室50
が開放されるため、圧力シ−ルや加圧構造が不要とな
り、また、搬送ベルト53を使った連続加熱殺菌が可能
になる。
Further, in this heat sterilizer, the left and right exhaust ducts 55 and 56 constantly discharge the superheated steam B2 supplied to the microwave heating chamber 50 by the amount. From this, the pressure of the superheated steam is slightly high (0.1 to 0.7K
g / cm 2 G) even if present, microwave heating chamber 50
Is opened, a pressure seal and a pressurizing structure are not required, and continuous heat sterilization using the conveyor belt 53 is possible.

【0038】次に、本発明の加熱殺菌方法をいて実際に
殺菌を行なった実験設備と実験デ−タについて述べる。 実験設備 〇 マイクロ波加熱装置 マイクロ波最大出力 : 0〜1.5KW×2台(0〜3KW) オ−ブン寸法 : 800W×830L×850Hmm 回転テ−ブル : 600φ スタラファン : 電波撹拌機 熱風循環発生機 : ヒ−タ−容量5KW(自動温調回路付) 耐熱循環ファン4m3/分 循環量:手動ダンパ−付 排 気 : φ100mm手動ダンパ−付 〇 過熱蒸気供給装置 ボイラ− : 最大蒸発量60kg/Hr 最大圧力5.5Kg/cm2G ス−パ−ヒ−タ− : ヒ−タ−容量6KW(自動温調回路付) 過熱蒸気圧力 最大0.7Kg/cm2G 〇 計 測 器 温度計 : 光ファイバ−温度計 安立計器 AMOTH FX8000 重量計 : SINKO DENSI SG−10K 〇 実験原料 実験例 1 品名 : 玄そば(そば殻付) 処理前菌数 : 2.8×106個/g 実験例 2 品名 : そば粉 処理前菌数 : 4.5×105個/g
Next, the experimental equipment and the experimental data for the actual sterilization using the heat sterilization method of the present invention will be described. Experimental equipment Microwave heating device Microwave maximum output: 0 to 1.5KW x 2 units (0 to 3KW) Oven dimensions: 800W x 830L x 850Hmm Rotation table: 600φ stirrer fan: Radio wave stirrer Hot air circulation generator : Heater capacity 5 kW (with automatic temperature control circuit) Heat-resistant circulation fan 4 m 3 / min Circulation amount: With manual damper Exhaust air: φ100 mm With manual damper 〇 Superheated steam supply boiler: Maximum evaporation amount 60 kg / Hr maximum pressure 5.5 Kg / cm 2 G scan - Pa - heat - data -: heat - data - capacity 6KW (with automatic temperature control circuit) superheated steam pressure up to 0.7 Kg / cm 2 G 〇 measuring instruments thermometer: light Fiber-thermometer Anritsu instrument AMOTH FX8000 Weighing scale: SINKO DENSI SG-10K 〇 Experimental raw material experiment example 1 Product name: Gen buckwheat (with buckwheat shell) Number of pre-treatment bacteria: 2.8 × 10 6 cells / g Experimental example 2 Product name: Number of bacteria before buckwheat treatment: 4.5 × 10 5 cells / g

【0039】実験デ−タ Experimental data

【数1】 [Equation 1]

【0040】実験結果 そば殻をかぶった玄そば全般において、また粉に引いた
そば粉の一番条件の厳しいそば粉Cにおいても、外観上
の色については、変色は見られず、そば粉に対する吸湿
はなく、むしろ若干乾燥気味で非常に良好な結果であっ
た。そば粉について実際にそばを打って、試食したが、
程々の香りと粘り具合も満足する結果が得られた。
Experimental Results No discoloration was observed in the appearance of buckwheat flour in the whole buckwheat flour covered with buckwheat flour, and also in buckwheat flour C, which is the most severe condition of buckwheat flour drawn into flour. There was no moisture absorption and rather a slight dryness, which was a very good result. About buckwheat flour I actually smashed soba and tried it,
The result was that the scent and tenacity were moderate.

【0041】[0041]

【発明の効果】上記した通り、本発明に係る加熱殺菌方
法によれば、マイクロ波加熱室内を大気圧に近い圧力の
過熱蒸気の雰囲気下に被殺菌物を配置し、この被殺菌物
にマイクロ波を照射して殺菌することから、被殺菌物の
内外から急速加熱して殺菌することができる。
As described above, according to the heat sterilization method of the present invention, the substance to be sterilized is placed in the microwave heating chamber under the atmosphere of superheated steam having a pressure close to the atmospheric pressure, and the substance to be sterilized Since sterilization is performed by irradiating waves, it is possible to rapidly sterilize the object to be sterilized by heating it from inside and outside.

【0042】この結果、高速殺菌できる他、熱に敏感な
食品や外形がパウジ或いは成形容器で包装された食品に
ついても充分な殺菌を行なうことができる。
As a result, in addition to high-speed sterilization, heat-sensitive foods and foods whose outer shape is packaged in a pauge or molded container can be sufficiently sterilized.

【0043】また、過熱蒸気を使用しても加圧構造とな
らないので、圧力構造やシ−ル対策を必要としないか
ら、この面でコスト、管理、安全性に有利な加熱殺菌方
法となる。
Further, even if the superheated steam is used, the pressurizing structure is not formed, so that there is no need for a pressure structure or a seal countermeasure, and in this respect, the heat sterilization method is advantageous in cost, management and safety.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の加熱殺菌方法の一実施形態を示す加熱
殺菌装置を示す機構図である。
FIG. 1 is a mechanism diagram showing a heat sterilization apparatus showing an embodiment of a heat sterilization method of the present invention.

【符号の説明】[Explanation of symbols]

50 マイクロ波加熱室 53 搬送ベルト 55、56 排気ダクト 57 ボイラ 58 仕切弁 59 減圧弁 60 加熱ヒ−タ− 63a、63b、63c・・・・・過熱蒸気の吹出口 64 循環ファン 65 加熱ヒ−タ− 67 マイクロ波発振機 A 被殺菌物 B1 飽和水蒸気 B2 過熱蒸気 50 microwave heating chamber 53 Conveyor belt 55, 56 Exhaust duct 57 Boiler 58 Gate valve 59 Pressure reducing valve 60 heating heater 63a, 63b, 63c ... Outlet of superheated steam 64 circulation fan 65 heating heater 67 Microwave oscillator A sterilizer B1 saturated steam B2 superheated steam

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 マイクロ波加熱室内でマイクロ波エネル
ギ−と水蒸気エネルギ−とを被殺菌物に与えて殺菌する
加熱殺菌方法において、水蒸気の圧力を大気圧近くまで
減圧すると共に、この水蒸気の温度を110〜300℃
程度まで昇温してマイクロ波加熱室内を過熱蒸気の雰囲
気状態とし、被殺菌物にマイクロ波と水蒸気とを与えて
加熱殺菌することを特徴とする加熱殺菌方法。
1. In a heat sterilization method in which microwave energy and water vapor energy are applied to an object to be sterilized in a microwave heating chamber, the pressure of the water vapor is reduced to near atmospheric pressure and the temperature of the water vapor is controlled. 110-300 ° C
A heat sterilization method comprising heating to a certain degree to bring the inside of a microwave heating chamber into an atmosphere of superheated steam, and applying microwaves and steam to an object to be sterilized for heat sterilization.
【請求項2】 マイクロ波室内に熱風を送り、マイクロ
波加熱室内の雰囲気である過熱蒸気を保温することを特
徴とする請求項1記載の加熱殺菌方法。
2. The heat sterilization method according to claim 1, wherein hot air is sent into the microwave chamber to keep the superheated steam as an atmosphere in the microwave heating chamber warm.
JP10246540A 1998-08-18 1998-08-18 Thermal sterilization Pending JP2000060511A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10246540A JP2000060511A (en) 1998-08-18 1998-08-18 Thermal sterilization

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10246540A JP2000060511A (en) 1998-08-18 1998-08-18 Thermal sterilization

Publications (1)

Publication Number Publication Date
JP2000060511A true JP2000060511A (en) 2000-02-29

Family

ID=17149938

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10246540A Pending JP2000060511A (en) 1998-08-18 1998-08-18 Thermal sterilization

Country Status (1)

Country Link
JP (1) JP2000060511A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014077555A (en) * 2012-10-09 2014-05-01 Kiyotsune Shino Microwave high temperature heater
JP2014117164A (en) * 2012-12-13 2014-06-30 Nisshin Seifun Group Inc Continuous steam sterilization device
KR101849847B1 (en) * 2016-08-30 2018-04-18 동서식품주식회사 Method and apparatus for sterilizing foods by using hot wind and microwave
US11229095B2 (en) 2014-12-17 2022-01-18 Campbell Soup Company Electromagnetic wave food processing system and methods

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014077555A (en) * 2012-10-09 2014-05-01 Kiyotsune Shino Microwave high temperature heater
JP2014117164A (en) * 2012-12-13 2014-06-30 Nisshin Seifun Group Inc Continuous steam sterilization device
US11229095B2 (en) 2014-12-17 2022-01-18 Campbell Soup Company Electromagnetic wave food processing system and methods
KR101849847B1 (en) * 2016-08-30 2018-04-18 동서식품주식회사 Method and apparatus for sterilizing foods by using hot wind and microwave

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