JP2644063B2 - Manufacturing method of retort food - Google Patents

Manufacturing method of retort food

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Publication number
JP2644063B2
JP2644063B2 JP8038390A JP8038390A JP2644063B2 JP 2644063 B2 JP2644063 B2 JP 2644063B2 JP 8038390 A JP8038390 A JP 8038390A JP 8038390 A JP8038390 A JP 8038390A JP 2644063 B2 JP2644063 B2 JP 2644063B2
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JP
Japan
Prior art keywords
food
container
sterilization
pressure
internal pressure
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 - Fee Related
Application number
JP8038390A
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Japanese (ja)
Other versions
JPH03277261A (en
Inventor
英文 岡本
浩次 仙石
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HAUSU SHOKUHIN KK
Original Assignee
HAUSU SHOKUHIN KK
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Priority to JP8038390A priority Critical patent/JP2644063B2/en
Publication of JPH03277261A publication Critical patent/JPH03277261A/en
Application granted granted Critical
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Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、レトルト食品の製造方法に関する。Description: TECHNICAL FIELD The present invention relates to a method for producing a retort food.

(従来の技術) 特開昭61−63271号公報には、耐熱性容器中に食品を
空気を残したまま充填、密封し、これを加圧状態の100
℃以上の湯中で回転又は反転させながら加熱した後、加
圧状態の冷水中で冷却することにより、食品の殺菌が十
分に行え、かつ食品が変色することがないレトルト食品
の製造方法が開示されている。
(Prior Art) JP-A-61-63271 discloses that a food is filled and sealed in a heat-resistant container while leaving air therein, and the food is sealed under pressure.
After heating while rotating or inverting in hot water of at least ℃, by cooling in cold water in a pressurized state, sterilization of food can be sufficiently performed, and a method for producing a retort food without discoloration of food is disclosed. Have been.

この方法では、容器内に空気を残存させているので、
殺菌中容器内の空気の移動によって食品が撹拌され、こ
れによって食品への伝熱が促進されて殺菌効率が向上す
るという利点がある。そして、この利点を得るために
は、通常容器内に5%以上の含気が必要である。しかし
ながら、このような状態で容器内に空気が残存すると、 殺菌中空気の存在で食品が変色する、 保存中の食品の劣化が促進される、 運搬時等に容器が破損しやすくなる、 という問題がある。
In this method, since air is left in the container,
There is an advantage that the food is stirred by the movement of the air in the container during the sterilization, whereby heat transfer to the food is promoted and the sterilization efficiency is improved. And, in order to obtain this advantage, it is usually necessary that the container contains 5% or more of air. However, if air remains in the container in such a state, the discoloration of the food due to the presence of the air during sterilization, the deterioration of the food during storage is promoted, and the container is easily damaged during transportation etc. There is.

(発明の解決しようとする課題) 従って、本発明は、前記の問題を解消して、殺菌効率
のよいレトルト食品の製造方法を提供することを目的と
する。
(Problems to be Solved by the Invention) Accordingly, an object of the present invention is to solve the above-mentioned problems and to provide a method for producing a retort food with high sterilization efficiency.

(課題を解決するための手段) 本発明は、レトルト釜の内圧を容器の内圧よりもやや
低くして、両者に一定の圧力差を保ちながら回転式の加
圧加熱殺菌処理を行うと、殺菌中容器内で食品中の水分
が気化した蒸気によって食品が撹拌され、食品への伝熱
が促進されて殺菌効率が向上するとの知見に基いてなさ
れたものである。
(Means for Solving the Problems) The present invention provides a sterilization method in which the internal pressure of a retort pot is slightly lower than the internal pressure of a container, and a rotary pressurized heat sterilization treatment is performed while maintaining a constant pressure difference between the two. The food is agitated by the vaporized water in the food in the middle container, the heat transfer to the food is promoted, and the sterilization efficiency is improved.

即ち、本発明は、可撓性の耐熱容器に該容器の最大容
積に満たない量の高水分の液状若しくはペースト状の食
品を含気率2%以下で密封収容し、該容器の加圧加熱殺
菌処理を、殺菌装置の内圧を容器の内圧よりもやや低く
して両者に一定の圧力差を保ちながら、かつ該容器を回
転及び/又は反転させ、食品中の水分が気化した蒸気に
よって食品を撹拌して行うことを特徴とするレトルト食
品の製造方法である。
In other words, the present invention provides a flexible heat-resistant container in which a liquid or paste food having a high water content less than the maximum volume of the container is hermetically contained at an air content of 2% or less, and the container is heated under pressure. In the sterilization process, the internal pressure of the sterilizer is slightly lower than the internal pressure of the container, while maintaining a constant pressure difference between the two, and the container is rotated and / or inverted, and the food in the food is vaporized by the vaporized water in the food. A method for producing a retort food, which is performed by stirring.

容器としては、可撓性の耐熱容器を用いる。可撓性の
容器とは、容器の最大容積に満たない量の食品を含気を
少なくした状態で密封収容することができる柔軟な容器
を意味する。このような容器としては、レトルトパウチ
等の袋状容器、合成樹脂等の可撓材からなるカップ状容
器等が挙げられる。特に、従来の殺菌処理では、容量が
500cc以上の容器を用いると、長時間加熱を要し、食品
の品質劣化が問題となっていた。しかし、本発明では、
下記の殺菌処理により殺菌効率が向上するため、このよ
うな大容量の容器を用いても上記の問題が顕在化しな
い。従って、上記大容量の容器を好適に用いることがで
きる。
As the container, a flexible heat-resistant container is used. By flexible container is meant a flexible container capable of hermetically containing less than the container's maximum volume of food with reduced aeration. Examples of such a container include a bag-shaped container such as a retort pouch and a cup-shaped container made of a flexible material such as a synthetic resin. In particular, in the conventional sterilization treatment, the capacity is
When a container of 500 cc or more is used, heating is required for a long time, and deterioration of food quality has been a problem. However, in the present invention,
Since the sterilization efficiency is improved by the following sterilization treatment, even if such a large-capacity container is used, the above problem does not appear. Therefore, the large-capacity container can be suitably used.

食品としては、液状若しくはペースト状のものを用
い、水分の多いものが好ましい。特に食品は、粘度1000
0cp以下、好ましくは6000cp以下のものを用いるのがよ
い。これは、粘度が10000cpを越えると、殺菌処理を下
記する本発明の方法で行っても、殺菌中食品から気化し
た蒸気によって食品を十分に撹拌することができず、所
望の殺菌効率が得られない場合があるからである。従っ
て、上記の食品の粘度によって、十分な殺菌効率を得る
ことができる。尚、本発明において、粘度とは、60℃に
おける食品の粘度をB型粘度計で測定したものである。
食品の種類としては、スープ、シチュー、カレー或いは
これらに具を含むものが例示される。
As the food, a liquid or paste-like food is used, and a food having a high moisture content is preferable. In particular, food has a viscosity of 1000
0 cp or less, preferably 6000 cp or less is used. This is because when the viscosity exceeds 10,000 cp, even if the sterilization treatment is performed by the method of the present invention described below, the food cannot be sufficiently stirred by the vaporized vapor from the food being sterilized, and the desired sterilization efficiency is obtained. This is because there may be no case. Therefore, sufficient sterilization efficiency can be obtained depending on the viscosity of the food. In the present invention, the viscosity is a value obtained by measuring the viscosity of a food at 60 ° C. with a B-type viscometer.
Examples of food types include soups, stews, curries, and foods containing these ingredients.

上記の食品を、容器の内部に含気率2%以下、好まし
くは0.8%以下〜満注の状態で収容密封する。含気率が
2%を越えると前記の含気による問題が顕在化しやす
い。本発明の特有の差圧式殺菌処理では、上記の範囲の
含気率で十分な殺菌効率を得ることができ、従って、前
記の含気による問題が発生し難い。
The above-mentioned food is housed and sealed in a container with an air content of 2% or less, preferably 0.8% or less to full filling. If the air content exceeds 2%, the above-mentioned problems due to air content are likely to become apparent. In the differential pressure sterilization treatment unique to the present invention, a sufficient sterilization efficiency can be obtained at an air content in the above range, and therefore, the problem caused by the air impairment hardly occurs.

次に、本発明の殺菌処理方法を説明する。 Next, the sterilization treatment method of the present invention will be described.

前記の食品を収容した容器を、殺菌装置の内圧を容器
の内圧よりもやや低くして両者に一定の圧力差を保ちな
がら加圧加熱殺菌処理する。つまり、このようにして殺
菌処理を行うと、殺菌中容器内で食品中の水分が気化し
た蒸気によって食品が撹拌され、食品への伝熱が促進さ
れるため、殺菌効率が向上するのである。
The container containing the food is subjected to pressure and heat sterilization while keeping the internal pressure of the sterilizer slightly lower than the internal pressure of the container and maintaining a constant pressure difference between the two. That is, when the sterilization treatment is performed in this manner, the food is stirred by the vaporized water in the food in the container during the sterilization, and the heat transfer to the food is promoted, so that the sterilization efficiency is improved.

上記の殺菌処理は、温度110〜135℃で2〜60分間、殺
菌装置内圧を、これと容器内圧との差圧(以下単に差圧
という)が1.0kg/cm2(ゲージ圧、本発明で圧力は全て
ゲージ圧を指す)以下となるように調整して行うのがよ
い。この場合の殺菌装置の内圧は0〜2.0kg/cm2が好ま
しい。更に好ましくは、温度110〜125℃で10〜60分間、
差圧0.1〜0.5kg/cm2に保ちながら行うのがよい。この場
合の殺菌装置の内圧は0.1〜1.2kg/cm2が好ましい。差圧
がない場合は、殺菌中容器内で気化した蒸気による撹拌
効果とこれによる殺菌効率を得ることができない。一
方、上記各々の条件で差圧が数値範囲を越えると、殺菌
中容器が破損する等の問題が生じやすい。従って、上記
数値範囲の差圧によって、各々の条件で容器の破損等の
問題を伴わずに良好な殺菌効率を得ることができる。
The above sterilization treatment is performed at a temperature of 110 to 135 ° C. for 2 to 60 minutes by using the internal pressure of the sterilization apparatus, and the differential pressure between the internal pressure of the sterilizer and the internal pressure of the sterilizer (hereinafter simply referred to as differential pressure) is 1.0 kg / cm 2 (gauge pressure, in the present invention). (All pressures indicate gauge pressures). In this case, the internal pressure of the sterilizer is preferably 0 to 2.0 kg / cm 2 . More preferably, at a temperature of 110 to 125 ° C. for 10 to 60 minutes,
It is recommended to maintain the pressure difference between 0.1 kg / cm 2 and 0.5 kg / cm 2 . In this case, the internal pressure of the sterilizer is preferably 0.1 to 1.2 kg / cm 2 . If there is no differential pressure, it is not possible to obtain the stirring effect of the vapor vaporized in the container during sterilization and the sterilization efficiency due to this. On the other hand, if the differential pressure exceeds the numerical range under each of the above conditions, problems such as breakage of the container during sterilization are likely to occur. Therefore, with the pressure difference in the above numerical range, good sterilization efficiency can be obtained without any problem such as breakage of the container under each condition.

また、殺菌処理は、装置内圧0kg/cm2、温度80〜100
℃で2〜10分間、差圧を0.5kg/cm2以下に保ちながら行
う、装置内圧0〜0.6kg/cm2、温度100〜115℃で2〜1
0分間、差圧を0.5kg/cm2に保ちながら行う、装置内圧
0〜2.0kg/cm2、温度115〜135℃で1〜5分間、差圧を
1.0kg/cm2以下に保ちながら行う、以上〜の条件で
連続して行うことができる。数値限定の意味は、前記の
場合と同様である。
In addition, sterilization treatment is performed at a device internal pressure of 0 kg / cm 2 and a temperature of 80 to 100.
2 to 10 minutes at a pressure of 0.5 kg / cm 2 or less at an internal pressure of 0 to 0.6 kg / cm 2 at a temperature of 100 to 115 ° C. for 2 to 1
0 minutes, the differential pressure is maintained at 0.5 kg / cm 2 , the internal pressure of the apparatus is 0 to 2.0 kg / cm 2 , the temperature is 115 to 135 ° C., and the differential pressure is 1 to 5 minutes.
It can be carried out continuously under the above conditions, while keeping it at 1.0 kg / cm 2 or less. The meaning of the numerical limitation is the same as in the above case.

上記の殺菌処理は、レトルト釜等を使用し、過熱水蒸
気、熱風、油等の熱媒を用いて行えばよい。殺菌処理
は、耐熱性容器を回転及び/又は反転させながら行う。
これによって、容器内の蒸気による撹拌効果を高め、更
に良好な殺菌効率を得ることができる。上記の回転(反
転)式の殺菌処理は、例えば、容器をレトルト釜内に水
平方向の回転軸を中心に回転可能に設置されたリテーナ
に収容し、上記の回転軸を駆動しながら行えばよい。
尚、この場合に、容器が袋状であるとその横軸を、カッ
プ状であるとその縦軸又は横軸を、各々3〜45度、好ま
しくは5〜20度傾斜させた状態で回転(反転)させなが
ら殺菌処理を行うことが望ましい。こうすることによっ
て、殺菌中容器内で蒸気の移動が促進され、食品が撹拌
されて、更に高い殺菌効率が得られる。上記の方法を達
成するには、例えば、前記のレトルト釜内のリテーナの
容器を収容する部分の底壁の傾きを上記の範囲の角度に
すればよい。また、回転又は反転は、殺菌中に5〜50rp
mの回転速度で行うのがよい。
The above sterilization treatment may be performed using a retort pot or the like and using a heating medium such as superheated steam, hot air, or oil. The sterilization process is performed while rotating and / or inverting the heat-resistant container.
Thereby, the stirring effect by the steam in the container can be enhanced, and more favorable sterilization efficiency can be obtained. The above-mentioned rotation (reversal) type sterilization treatment may be performed, for example, by housing the container in a retainer rotatably installed around a horizontal rotation axis in a retort pot and driving the rotation axis. .
In this case, when the container is in the shape of a bag, the horizontal axis thereof is rotated, and when the container is in the shape of a cup, the vertical or horizontal axis is rotated by 3 to 45 degrees, preferably 5 to 20 degrees. It is desirable to perform the sterilization process while inverting. By doing so, the movement of steam in the container during sterilization is promoted, and the food is agitated, so that higher sterilization efficiency is obtained. In order to achieve the above method, for example, the inclination of the bottom wall of the portion of the retort pot that holds the container of the retainer may be set to an angle in the above range. Also, rotation or reversal is 5-50 rp during sterilization.
It is better to perform at a rotation speed of m.

本発明では、上記殺菌処理後、常法により容器内の食
品を冷却することができる。尚、冷却処理は、これが加
圧状態で行われる間は、前記の殺菌処理と同様にして差
圧を保ちながら行うことができる。この場合は、食品の
冷却効率を向上することができる。
In the present invention, after the above sterilization treatment, the food in the container can be cooled by an ordinary method. Note that the cooling process can be performed while maintaining the pressure difference in the same manner as in the above-described sterilization process, while the cooling process is performed in a pressurized state. In this case, the cooling efficiency of the food can be improved.

(発明の効果) 本発明の方法によれば、殺菌中容器内の気化した蒸
気で撹拌能力を得、これによって十分な殺菌効率を得る
ことができる、容器内には必要最小量の空気しか存在
しないので、殺菌中に空気によって食品が変色しない、
保存中に空気によって食品が劣化しない、運搬時等
に容器が破損しない、という優れた効果が得られる。
(Effect of the Invention) According to the method of the present invention, it is possible to obtain a stirring ability with the vaporized vapor in the container during sterilization, thereby obtaining sufficient sterilization efficiency. Only a minimum amount of air is required in the container. Do not discolor food during sterilization due to air,
An excellent effect is obtained that the food is not deteriorated by air during storage and the container is not damaged during transportation.

[実施例1] 水分含量85%、粘度約1000cpのスープ900gを、内容量
1000ccのレトルトパウチに満注し、密封した。上記のレ
トルトパウチをレトルト釜を使用して、過熱水蒸気によ
り釜内圧0〜1.1kg/cm2、温度122℃で20分間、差圧を0.
5kg/cm2以下に保ちながら回転式の加圧加熱殺菌処理を
行った。上記の殺菌処理後、レトルト釜内に冷却水を送
り、パウチを常温にまで冷却してレトルト食品を製造し
た。尚、殺菌処理乃至冷却処理の間、レトルト釜内のリ
テーナーを15rpmで一方方向に回転させた。
[Example 1] 900 g of a soup having a water content of 85% and a viscosity of about 1000 cp was used.
Fully filled into a 1000cc retort pouch and sealed. Using the above retort pouch in a retort pot, superheated steam is used to set the pressure inside the pot to 0 to 1.1 kg / cm 2 and a temperature of 122 ° C. for 20 minutes, with a differential pressure of 0.
While maintaining the pressure at 5 kg / cm 2 or less, a rotary pressurized heat sterilization treatment was performed. After the above sterilization treatment, cooling water was fed into the retort pot, and the pouch was cooled to room temperature to produce a retort food. During the sterilization treatment and the cooling treatment, the retainer in the retort pot was rotated in one direction at 15 rpm.

得られたレトルト食品は、常温で約2年間の保存が可
能であり、6カ月保存後に食したところ、スープは褪色
がなく、良好な風味を有していた。
The obtained retort food could be stored at room temperature for about 2 years, and after eating for 6 months, the soup had no fading and had a good flavor.

[実施例2] 水分含量83%、粘度約3000cpのスープ900gを、内容量
1000ccのレトルトパウチに満注し、密封した。このレト
ルトハウチを、レトルト釜内に水平方向の回転軸を中心
に回転可能に設置されたリテーナの収容部材(底壁の傾
き5度)に収容した。上記の装置を使用して、過熱水蒸
気より、釜内圧0kg/cm2、温度100℃で2分間、差圧を
0.1kg/cm2以下に保ちながら、続いて、釜内圧0〜0.4
kg/cm2、温度110℃で5分間、差圧を0.3kg/cm2以下に保
ちながら、続いて、釜内圧0.3〜0.8kg/cm2、温度120
℃で10分間、差圧を0.2〜0.5kg/cm2に保ちながら、以上
の〜の条件で連続して殺菌処理を行った。そして、
上記の殺菌処理の後、釜内に15℃の冷却水を送り、10分
間冷却処理してレトルト食品を得た。尚、殺菌処理乃至
冷却処理の間、リテーナーを15rpmで一方方向に回転さ
せた。
[Example 2] 900 g of a soup having a water content of 83% and a viscosity of about 3000 cp was used.
Fully filled into a 1000cc retort pouch and sealed. The retort house was housed in a housing member (5 degrees of inclination of the bottom wall) of a retainer which was installed in the retort pot so as to be rotatable around a horizontal rotation axis. Using the above equipment, the pressure difference from the superheated steam was set at 0 kg / cm 2 in the pot and at 100 ° C for 2 minutes.
While maintaining the pressure at 0.1 kg / cm 2 or less,
kg / cm 2, 5 min at a temperature 110 ° C., while maintaining the differential pressure 0.3 kg / cm 2 or less, followed by the kettle pressure 0.3~0.8kg / cm 2, temperature 120
The sterilization treatment was continuously performed at 10 ° C. for 10 minutes while maintaining the differential pressure at 0.2 to 0.5 kg / cm 2 under the above conditions. And
After the above sterilization treatment, cooling water at 15 ° C. was fed into the kettle and subjected to a cooling treatment for 10 minutes to obtain a retort food. The retainer was rotated in one direction at 15 rpm during the sterilization and cooling treatments.

得られたレトルト食品は、常温で約2年間の保存が可
能であり、6カ月保存後に食したところ、スープは褪色
がなく、良好な風味を有していた。
The obtained retort food could be stored at room temperature for about 2 years, and after eating for 6 months, the soup had no fading and had a good flavor.

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】可撓性の耐熱容器に該容器の最大容積に満
たない量の高水分の液状若しくはペースト状の食品を含
気率2%以下で密封収容し、該容器の加圧加熱殺菌処理
を、殺菌装置の内圧を容器の内圧よりもやや低くして両
者に一定の圧力差を保ちながら、かつ該容器を回転及び
/又は反転させ、食品中の水分が気化した蒸気によって
食品を撹拌して行うことを特徴とするレトルト食品の製
造方法。
1. A highly heat-resistant flexible container containing a liquid or paste food having a high water content less than the maximum volume of the container in an airtight condition at an air content of 2% or less, and pressurizing and heat sterilizing the container. In the treatment, the internal pressure of the sterilizer is slightly lower than the internal pressure of the container, and while maintaining a constant pressure difference between the two, the container is rotated and / or inverted, and the food is agitated by the vaporized water in the food. A method for producing a retort food.
【請求項2】食品が粘度10000cp以下の液状若しくはペ
ースト状のものである請求項1記載の方法。
2. The method according to claim 1, wherein the food is a liquid or paste having a viscosity of 10,000 cp or less.
【請求項3】加圧加熱殺菌処理を、温度110〜135℃で2
〜60分間、殺菌装置の内圧をこれと容器の内圧との差圧
が1.0kg/cm2以下となるように調整しながら行う請求項
1又は2記載の方法。
3. A pressure and heat sterilization treatment at a temperature of 110 to 135 ° C.
60 min, The method of claim 1 or 2, wherein the differential pressure between the internal pressure of which the container internal pressure of the sterilizing apparatus performs while adjusting so that 1.0 kg / cm 2 or less.
JP8038390A 1990-03-27 1990-03-27 Manufacturing method of retort food Expired - Fee Related JP2644063B2 (en)

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Application Number Priority Date Filing Date Title
JP8038390A JP2644063B2 (en) 1990-03-27 1990-03-27 Manufacturing method of retort food

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JPH03277261A JPH03277261A (en) 1991-12-09
JP2644063B2 true JP2644063B2 (en) 1997-08-25

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Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2645944B2 (en) * 1991-12-16 1997-08-25 ハウス食品株式会社 Method and apparatus for pressurized heat sterilization of filled soft packaging bags
JP2645945B2 (en) * 1991-12-16 1997-08-25 ハウス食品株式会社 Method and apparatus for cooling filled soft packaging bags
GB2432099A (en) * 2005-11-14 2007-05-16 Mars Inc Thermal stabilization of packaged foodstuffs
MY154025A (en) * 2007-08-10 2015-04-30 Toyo Seikan Group Holdings Ltd Method for sterilizing a liquid food filled in a pouch

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