JP3053529B2 - Sterilization and cooking of aerated foods - Google Patents
Sterilization and cooking of aerated foodsInfo
- Publication number
- JP3053529B2 JP3053529B2 JP6131398A JP13139894A JP3053529B2 JP 3053529 B2 JP3053529 B2 JP 3053529B2 JP 6131398 A JP6131398 A JP 6131398A JP 13139894 A JP13139894 A JP 13139894A JP 3053529 B2 JP3053529 B2 JP 3053529B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- food
- cooling water
- tank
- cooling
- 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
Links
- 235000013305 food Nutrition 0.000 title claims description 122
- 230000001954 sterilising effect Effects 0.000 title claims description 103
- 238000004659 sterilization and disinfection Methods 0.000 title claims description 79
- 238000010411 cooking Methods 0.000 title claims description 42
- 239000000498 cooling water Substances 0.000 claims description 73
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 56
- 238000001816 cooling Methods 0.000 claims description 28
- 238000000034 method Methods 0.000 claims description 21
- 238000010438 heat treatment Methods 0.000 claims description 19
- 230000008569 process Effects 0.000 claims description 13
- 239000011261 inert gas Substances 0.000 claims description 5
- 230000007704 transition Effects 0.000 description 13
- 238000002347 injection Methods 0.000 description 5
- 239000007924 injection Substances 0.000 description 5
- 230000001105 regulatory effect Effects 0.000 description 4
- 238000007789 sealing Methods 0.000 description 4
- 230000001276 controlling effect Effects 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 206010016952 Food poisoning Diseases 0.000 description 1
- 208000019331 Foodborne disease Diseases 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000003899 bactericide agent Substances 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- BEFDCLMNVWHSGT-UHFFFAOYSA-N ethenylcyclopentane Chemical compound C=CC1CCCC1 BEFDCLMNVWHSGT-UHFFFAOYSA-N 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003755 preservative agent Substances 0.000 description 1
- 230000002335 preservative effect Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 229940075582 sorbic acid Drugs 0.000 description 1
- 235000010199 sorbic acid Nutrition 0.000 description 1
- 239000004334 sorbic acid Substances 0.000 description 1
- 238000009461 vacuum packaging Methods 0.000 description 1
Landscapes
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
- General Preparation And Processing Of Foods (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、含気食品の殺菌および
加熱調理法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for sterilizing and heating an aerated food.
【0002】[0002]
【従来の技術】従来、含気食品の殺菌処理においては、
調理済の食品または所定の段階まで調理した半調理の食
材を、気体バリヤー性の優れた積層シートからなる袋
(レトルトパウチ)または防錆処理した缶等に収納し、
これらの袋内または缶内の空気を不活性ガスに置換し、
袋口を熱シール加工により密封したり、缶をシール機に
より密封し、この状態で殺菌槽に収容し、殺菌槽に熱水
または加熱蒸気を送り、袋内または缶内の食材を殺菌処
理する方法が取られている。殺菌処理の効果を上げるた
め、また食材の味や形状を保ち食品の品質を保つために
は、高温で且つ短時間の処理が望ましく、一般に食材の
中心部で120℃4分(F値4)の加熱殺菌処理が標準
とされている。従来の殺菌法では、殺菌槽内に熱水を充
填し、これに含気食品を浸漬するか、または殺菌槽を加
圧した状態で含気食品に熱水や加熱蒸気を噴射して加熱
するのであるが、殺菌効果を確実にするために、加熱時
間は長く取っている。例えば、食品により100〜12
0℃近傍の温度で10〜60分位の時間をかけて殺菌処
理している。殺菌処理の加熱時間が長いと、缶やレトル
トパウチの独特な匂いが食品について食品の味や匂いを
損なったり、食品を半調理状態で出荷しようとしても長
時間の加熱により調理の段階が進んでしまったり、食品
が変形して外観を損なう等の問題がある。逆に加熱時間
を短くすると、食中毒の原因となる細菌に対して充分な
殺菌効果を上げることができないため、3%過酸化水素
やソルビン酸等の殺菌剤や保存材を併用したり、真空包
装等の対策を行なうことにより、殺菌効果を補わなけれ
ばならないという問題点を生じる。2. Description of the Related Art Conventionally, in the sterilization treatment of aerated foods,
Store the cooked food or semi-cooked ingredients cooked to a predetermined stage in a bag (retort pouch) made of a laminated sheet with excellent gas barrier properties or a rust-proof can, etc.
Replace the air in these bags or cans with inert gas,
The bag mouth is sealed by heat sealing, or the can is sealed with a sealing machine. In this state, the bag is stored in a sterilization tank, and hot water or heated steam is sent to the sterilization tank to sterilize food in the bag or the can. The way has been taken. In order to enhance the effect of the sterilization treatment, and to maintain the taste and shape of the food and maintain the quality of the food, high-temperature and short-time treatment is desirable. In general, 120 ° C. for 4 minutes at the center of the food (F value 4) Heat sterilization is standard. In the conventional sterilization method, hot water is filled in a sterilization tank, and the aerated food is immersed in the hot water, or hot water or heated steam is injected into the aerated food in a state where the sterilization tank is pressurized and heated. However, in order to ensure the sterilizing effect, the heating time is long. For example, depending on the food, 100 to 12
Sterilization treatment is performed at a temperature near 0 ° C. for about 10 to 60 minutes. If the heating time of the sterilization process is long, the unique smell of cans and retort pouches impairs the taste and smell of the food, and even if you try to ship the food in a partially cooked state, the cooking stage will progress due to long heating. There is a problem that the food is deformed and the appearance is impaired. Conversely, if the heating time is shortened, it will not be possible to achieve a sufficient bactericidal effect on bacteria that cause food poisoning. Therefore, a bactericide or preservative such as 3% hydrogen peroxide or sorbic acid is used together, or vacuum packaging is performed. By taking such measures, there is a problem that the sterilizing effect must be compensated.
【0003】[0003]
【発明が解決しようとする課題】前記従来の問題点を解
決するため、本発明では、高い温度で短時間に確実に殺
菌処理することにより殺菌処理の加熱時間を短縮し、食
品の外観、食品の味や匂いを損なうことない含気食品の
殺菌および加熱調理法を提供することを目的としてい
る。SUMMARY OF THE INVENTION In order to solve the above-mentioned conventional problems, the present invention reduces the heating time of the sterilization process by reliably performing the sterilization process at a high temperature in a short time, thereby reducing the appearance and the food quality of the food. It is an object of the present invention to provide a method for sterilizing and heating an air-containing food without impairing the taste and smell of the food.
【0004】[0004]
【課題を解決する手段】上記目的を達成するため、本発
明では、耐熱性容器に調理未完了の食品を充填し、容器
内を不活性ガス置換して密封した含気食品を殺菌槽に収
容し、この食品の中心温度を次の(1)乃至(5)の工
程順に多段階に変動することを特徴とする含気食品の殺
菌及び加熱調理法。 (1) 食品の中心温度を、5〜15分の間に80〜1
00℃まで急速に昇温する1次昇温工程、 (2) 前記80〜100℃までの食品の中心温度を、
含気食品の種類と量に基づく所定時間の間保持する調理
恒温工程、 (3) 食品の中心温度を、食品殺菌温度110〜12
0℃まで昇温する2次昇温工程、 (4) 前記110〜120℃までの食品の中心温度
を、2〜10分保持する殺菌処理工程、 (5) 冷却水槽を複数設け、該冷却水槽内の冷却水を
冷却し、該いずれか1つの冷却水槽内の冷却水を殺菌槽
内に注水して前記食品の中心温度を4〜15分で急速に
常温に下げた後、冷却に使用した冷却水を冷却水槽に回
収し冷却するとともに、次の冷却のときには前回と別の
冷却水槽内の冷却水を使用する冷却工程。In order to achieve the above object, according to the present invention, a heat-resistant container is filled with uncooked food, the inside of the container is replaced with an inert gas, and the sealed aerated food is stored in a sterilization tank. A method of sterilizing and heating an aerated food, wherein the center temperature of the food is changed in multiple stages in the order of the following steps (1) to (5). (1) Set the center temperature of the food to 80 to 1 in 5 to 15 minutes.
A primary temperature raising step of rapidly raising the temperature to 00 ° C., (2) the central temperature of the food to 80 to 100 ° C.,
A cooking constant temperature step of maintaining for a predetermined time based on the type and amount of the aerated food; (3) setting the central temperature of the food to a food sterilization temperature of 110 to 12;
A secondary temperature raising step of raising the temperature to 0 ° C., (4) a sterilizing step of maintaining the center temperature of the food to 110 to 120 ° C. for 2 to 10 minutes, (5) a plurality of cooling water tanks, The cooling water in the inside was cooled, the cooling water in any one of the cooling water tanks was poured into the sterilization tank, and the central temperature of the food was rapidly lowered to room temperature in 4 to 15 minutes, and then used for cooling. A cooling process in which cooling water is collected in a cooling water tank and cooled, and for the next cooling, cooling water in another cooling water tank is used.
【0005】また、食品の中心温度を次の(1)乃至
(6)の工程順に多段階に変動するようにした。 (1) 食品の中心温度を、5〜15分の間に80〜1
00℃まで急速に昇温する1次昇温工程、 (2) 前記80〜100℃までの食品の中心温度を、
含気食品の種類と量に基づく所定時間の間保持する調理
恒温工程、 (3) 食品の中心温度を、食品殺菌温度110〜12
0℃まで昇温する2次昇温工程、 (4) 前記110〜120℃までの食品の中心温度
を、2〜10分保持する殺菌処理工程、 (5) 前記食品の中心温度を、さらに122〜124
℃までに急速に上げ、ほぼ1分保持する高温殺菌処理工
程、 (6) 冷却水槽を複数設け、該冷却水槽内の冷却水を
冷却し、該いずれか1つの冷却水槽内の冷却水を殺菌槽
内に注水して前記122〜124℃の食品の中心温度を
4〜15分で急速に常温に下げた後、冷却に使用した冷
却水を冷却水槽に回収し冷却するとともに、次の冷却の
ときには前回と別の冷却水槽内の冷却水を使用する冷却
工程。Further, the center temperature of the food is varied in multiple stages in the order of the following steps (1) to (6). (1) Set the center temperature of the food to 80 to 1 in 5 to 15 minutes.
A primary temperature raising step of rapidly raising the temperature to 00 ° C., (2) the central temperature of the food to 80 to 100 ° C.,
A cooking constant temperature step of maintaining for a predetermined time based on the type and amount of the aerated food; (3) setting the central temperature of the food to a food sterilization temperature of 110 to 12;
(4) a sterilization process in which the center temperature of the food up to 110 to 120 ° C. is maintained for 2 to 10 minutes; and (5) a center temperature of the food in addition to 122. ~ 124
(C) A plurality of cooling water tanks are provided, the cooling water in the cooling water tank is cooled, and the cooling water in one of the cooling water tanks is sterilized. After pouring water into the tank and rapidly lowering the central temperature of the food at 122 to 124 ° C. to normal temperature in 4 to 15 minutes, the cooling water used for cooling is collected in a cooling water tank and cooled, and the next cooling is performed. Sometimes a cooling process that uses cooling water in a different cooling water tank from the previous one.
【0006】さらに、食品の中心温度を次の(1)乃至
(7)の工程順に多段階に変動するようにした。 (1) 食品の中心温度を、5〜15分の間に80〜1
00℃まで急速に昇温する1次昇温工程、 (2) 前記80〜100℃までの食品の中心温度を、
含気食品の種類と量に基づく所定時間の間保持する調理
恒温工程、 (3) 食品の中心温度を、3〜4分の間にほぼ110
℃まで急速に昇温する追加調理工程、 (4) 食品の中心温度を、食品殺菌温度120℃まで
昇温する2次昇温工程、 (5) 前記食品の中心温度を、3〜4分保持する殺菌
処理工程、 (6) 前記食品の中心温度を、さらに122〜124
℃に急速に上げ、ほぼ1分保持する高温殺菌処理工程、 (7) 冷却水槽を複数設け、該冷却水槽内の冷却水を
冷却し、該いずれか1つの冷却水槽内の冷却水を殺菌槽
内に注水して前記食品の中心温度を4〜15分で急速に
常温に下げた後、冷却に使用した冷却水を冷却水槽に回
収し冷却するとともに、次の冷却のときには前回と別の
冷却水槽内の冷却水を使用する冷却工程。Further, the center temperature of the food is changed in multiple stages in the order of the following steps (1) to (7). (1) Set the center temperature of the food to 80 to 1 in 5 to 15 minutes.
A primary temperature raising step of rapidly raising the temperature to 00 ° C., (2) the central temperature of the food to 80 to 100 ° C.,
(3) keeping the center temperature of the food at about 110 in 3 to 4 minutes, wherein the cooking temperature is maintained for a predetermined time based on the type and amount of the aerated food;
Additional cooking step of rapidly raising the temperature to 0 ° C., (4) secondary temperature raising step of raising the central temperature of the food to the food sterilization temperature of 120 ° C., (5) maintaining the central temperature of the food for 3 to 4 minutes (6) The central temperature of the food is further increased by 122 to 124.
° C, and a high-temperature sterilization treatment step of rapidly raising the temperature to about 1 minute, and (7) providing a plurality of cooling water tanks, cooling the cooling water in the cooling water tank, and dissolving the cooling water in any one of the cooling water tanks After the water is poured into the chiller and the center temperature of the food is rapidly lowered to room temperature in 4 to 15 minutes, the cooling water used for cooling is collected in a cooling water tank and cooled, and the next cooling is different from the previous cooling. Cooling process using cooling water in the water tank.
【0007】[0007]
【作用】以上のように、多段階で昇温(食品の中心温度
を調理温度まで上げた後、さらに殺菌温度に昇温)する
ので、殺菌温度に至るまでの時間が短く、食品を長時間
殺菌温度にさらすことによる食品の変質を防止できる。
しかも、冷却水槽内で充分に冷却した冷却水を殺菌槽に
注水で、食品を急速に常温に下げることができ、長時間
殺菌温度にさらすことによる食品の味や匂いの低下を防
げる。また、冷却に使用する冷却水は冷却水槽を交互に
使用することにより、回収し冷却水槽内で充分に冷却し
再使用できる。 [Action] As described above, the temperature is raised in multiple stages (the central temperature of the food
To the cooking temperature and then to the sterilization temperature)
So the time to reach the sterilization temperature is short and the food
Deterioration of food due to exposure to sterilization temperature can be prevented.
Moreover, the cooling water sufficiently cooled in the cooling water tank is transferred to the sterilization tank.
With water injection, food can be rapidly cooled to room temperature,
Prevents the taste and smell of food from being reduced by exposure to sterilization temperatures
I can. In addition, the cooling water used for cooling alternates the cooling water tank.
By using it, collect and cool it sufficiently in the cooling water tank.
Can be reused.
【0008】[0008]
【実施例】本発明の実施例を添付図面を参照して詳細に
説明する。図1は、本発明を実現する含気食品の殺菌お
よび調理システムの構成を示すブロック図で、この殺菌
および調理システムは、アルミパウチまたはアルミ缶等
に未調理または半調理の食品を入れ、不活性ガスにより
置換し密封した含気食品を収容し殺菌と調理を行う殺菌
槽6、供給された蒸気をさらに加熱する過熱蒸気発生装
置2、殺菌槽6に送る熱水に熱交換する熱交換器3、循
環ポンプ5、殺菌槽内の気圧を調整する気圧調整部、調
理殺菌した食品を取り出せる温度まて冷却する冷却部、
それらを制御する各種調整弁および制御盤24から構成
している。DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described in detail with reference to the accompanying drawings. FIG. 1 is a block diagram showing a configuration of a sterilization and cooking system for aerated foods that realizes the present invention. A sterilization tank 6 for accommodating and sealing sterilized and cooked air-containing foods replaced with an active gas, a superheated steam generator 2 for further heating the supplied steam, and a heat exchanger for exchanging heat with hot water sent to the sterilization tank 6. 3, a circulation pump 5, an air pressure adjusting unit for adjusting the air pressure in the sterilizing tank, a cooling unit for cooling down to a temperature at which the cooked and sterilized food can be taken out,
It is composed of various control valves for controlling them and a control panel 24.
【0009】以下この殺菌および調理システムの運転制
御を詳細に説明する。加熱蒸気を供給するボイラー(図
示せず)から蒸気調整アナログ弁1と過熱蒸気発生装置
2を介して加熱蒸気が熱交換器3の1次側に供給され、
熱交換器3の2次側を循環する熱水に熱交換し、熱水は
2方向切換弁4aを介して循環ポンプ5により殺菌槽6
内に噴出し、殺菌槽6に収容した含気食品に注ぎ、熱交
換した熱水は殺菌槽6の底部に溜まり、排水弁7を経て
還流管路21により熱交換器3の2次側に戻り、再び加
熱されて循環ポンプ5により繰り返し循環する。Hereinafter, the operation control of the sterilization and cooking system will be described in detail. Heated steam is supplied from a boiler (not shown) for supplying heated steam to the primary side of the heat exchanger 3 via a steam regulating analog valve 1 and a superheated steam generator 2,
The heat is exchanged with the hot water circulating on the secondary side of the heat exchanger 3, and the hot water is disinfected by the circulating pump 5 through the two-way switching valve 4a.
The hot water that has been injected into the sterilized tank 6 and poured into the sterilized tank 6 and heat-exchanged accumulates at the bottom of the sterilized tank 6, passes through the drain valve 7, and is returned to the secondary side of the heat exchanger 3 by the return line 21. It returns, is heated again, and is repeatedly circulated by the circulation pump 5.
【0010】殺菌槽6は筐体を耐圧構造とし、その前面
には含気食品を多段に載置した台車13を出し入れする
密閉扉(図示せず)が形成され、槽内の左右両側には熱
水を噴出する注水容器14が配設され、左右の注水容器
14のそれぞれ内側に向いた面には突出した複数のノズ
ル(図示せず)が設けられ、横長の開口を有するノズル
から噴出した熱水は台車13上の含気食品に帯状の流れ
となり注がれる。殺菌槽6の天井には槽内の空気圧を調
整する空気圧力管15を設けられ、コンプレッサ16に
より圧力調整アナログ弁17を介して空気圧を上昇さ
せ、槽内に配設した圧力センサ18により槽内の空気圧
を検出して制御盤24に送り、圧力調整アナログ弁17
と排気アナログ弁19を操作して、槽内の空気圧を熱水
温度に対応した所定の空気圧に保持している。The sterilization tank 6 has a housing having a pressure-resistant structure, and a sealing door (not shown) is formed on the front surface thereof for inserting and removing a cart 13 on which air-containing food is loaded in multiple stages. A water injection container 14 for jetting out hot water is provided, and a plurality of nozzles (not shown) protruding are provided on the inner surfaces of the left and right water injection containers 14, respectively. The hot water is poured into the aerated food on the trolley 13 as a belt-like flow. An air pressure pipe 15 for adjusting the air pressure in the tank is provided on the ceiling of the sterilizing tank 6, the air pressure is increased by a compressor 16 via a pressure adjusting analog valve 17, and the pressure in the tank is increased by a pressure sensor 18 disposed in the tank. The air pressure is detected and sent to the control panel 24, and the pressure adjusting analog valve 17
And the exhaust analog valve 19 are operated to maintain the air pressure in the tank at a predetermined air pressure corresponding to the hot water temperature.
【0011】過熱蒸気発生装置2は、装置内を通過する
加熱蒸気を別の熱源例えば熱交換機構を具えた電気ヒー
タ等により再度加熱して高温の加熱蒸気とし、熱交換器
3の1次側に高温の加熱蒸気を供給し、2次側を流れる
熱水に熱交換して高温の熱水を生成し、循環ポンプ5に
より殺菌槽内に送られる。この装置は、耐熱性の良いシ
リコーンオイル等を充填した筐体内に蒸気を流通するス
パイラル状またはU字状のパイプを貫通させ、筐体内に
電気ヒータ等の熱源を埋設し、シリコーンオイル等を介
して流通する蒸気を再加熱する装置で、電気ヒータを制
御することにより、所定過熱度の蒸気を生成する。The superheated steam generator 2 reheats the heated steam passing through the inside of the device by another heat source, for example, an electric heater equipped with a heat exchange mechanism or the like to produce high-temperature heated steam, and the primary side of the heat exchanger 3 Is supplied to the hot water, and heat is exchanged with hot water flowing on the secondary side to generate high-temperature hot water, which is sent into the sterilization tank by the circulation pump 5. In this device, a spiral or U-shaped pipe through which steam flows is penetrated into a housing filled with silicone oil or the like having good heat resistance, and a heat source such as an electric heater is buried in the housing. A device that reheats steam flowing through the heater and controls the electric heater to generate steam having a predetermined degree of superheat.
【0012】過熱した蒸気を熱交換器3に送り、熱交換
器3の2次側を循環する熱水の温度を上げ、この熱水を
循環ポンプ5により供給管路20を通して殺菌槽6の注
水容器14に送り、槽内に噴射し、含気食品を加熱して
調理および殺菌処理を行う。所定時間経過し加熱殺菌が
完了すると、2方向切換弁4aを切換えて熱水の流入を
止め、殺菌槽6内の熱水を2方向切換弁4bと開閉弁8
aを介して熱水回収タンク9に回収する。そして第1冷
却水槽10から冷却水管路11と2方向切換弁4aを通
して、循環ポンプ5により冷却水を殺菌槽6の注水容器
14から含気食品に注水し、注水した冷却水は殺菌槽6
の底に溜まり、排水弁7と2方向切換弁4bおよび開閉
弁8bを通って第1冷却水槽10に回収し、ついで第2
冷却水槽12から冷却水を送出する。このように交互に
第1冷却水槽10と第2冷却水槽12を切換えて循環さ
せるとともに、回収された冷却水をクーリングタワー等
により冷却して、含気食品を取り出せる温度になるまで
冷却する。The superheated steam is sent to the heat exchanger 3 to raise the temperature of hot water circulating on the secondary side of the heat exchanger 3, and this hot water is injected into the sterilization tank 6 through the supply pipe 20 by the circulation pump 5. It is sent to the container 14, injected into the tank, and heated and aerated to perform cooking and sterilization. When the heat sterilization is completed after a predetermined time has elapsed, the two-way switching valve 4a is switched to stop the flow of hot water, and the hot water in the sterilization tank 6 is discharged to the two-way switching valve 4b and the on-off valve 8
The hot water is recovered in the hot water recovery tank 9 through a. Then, cooling water is injected from the first cooling water tank 10 through the cooling water pipe 11 and the two-way switching valve 4a to the aerated food from the water supply container 14 of the sterilization tank 6 by the circulation pump 5, and the injected cooling water is supplied to the sterilization tank 6
Collected at the bottom of the first cooling water tank 10 through the drain valve 7, the two-way switching valve 4b, and the on-off valve 8b.
Cooling water is sent from the cooling water tank 12. In this way, the first cooling water tank 10 and the second cooling water tank 12 are alternately switched and circulated, and the collected cooling water is cooled by a cooling tower or the like, and cooled to a temperature at which the aerated food can be taken out.
【0013】熱交換器3の2次側に熱水温度を検出する
熱水温度センサ22を、殺菌槽内に槽内温度を検出する
槽内温度センサ23をそれぞれ設け、熱水温度および槽
内温度を検出して制御盤24にこの温度情報を送り、熱
水温度および槽内温度が予め食品ごとに設定された温度
時間推移曲線に沿って変化するように、過熱蒸気発生装
置2の運転と蒸気調整アナログ弁1の開口度を制御す
る。A hot water temperature sensor 22 for detecting hot water temperature is provided on the secondary side of the heat exchanger 3, and a tank temperature sensor 23 for detecting the tank temperature in the sterilizing tank. Detecting the temperature and sending this temperature information to the control panel 24, the operation of the superheated steam generator 2 and the operation of the superheated steam generator 2 are performed so that the hot water temperature and the tank temperature change along a temperature-time transition curve set in advance for each food. The opening degree of the steam control analog valve 1 is controlled.
【0014】熱水温度センサ22および槽内温度センサ
23からの温度情報が、温度時間推移曲線上の設定温度
より低い場合には、蒸気調整アナログ弁1の開閉度を拡
げ、同時に過熱蒸気発生装置2の電気ヒータを通電して
熱交換器3に送られる加熱蒸気の温度を上げ、熱交換器
3の二次側を循環する熱水の温度を上昇させる。他方、
槽内温度センサ27からの情報信号が温度時間推移曲線
上の設定温度より高い場合には、蒸気調整アナログ弁1
の開閉度を絞り、加熱蒸気の流量を下げるとともに、過
熱蒸気発生装置2の電気ヒータを切り、流通する蒸気の
温度を下げ、殺菌槽を循環する熱水の温度を下げ、槽内
温度を下げるようにして所定の調理および殺菌温度を保
持するようにしている。If the temperature information from the hot water temperature sensor 22 and the temperature sensor 23 inside the tank is lower than the set temperature on the temperature-time transition curve, the degree of opening and closing of the steam control analog valve 1 is increased, and at the same time, the superheated steam generator The electric heater 2 is energized to increase the temperature of the heating steam sent to the heat exchanger 3 and increase the temperature of the hot water circulating on the secondary side of the heat exchanger 3. On the other hand,
If the information signal from the in-bath temperature sensor 27 is higher than the set temperature on the temperature-time transition curve, the steam regulating analog valve 1
And the flow rate of the heated steam is reduced, the electric heater of the superheated steam generator 2 is turned off, the temperature of the flowing steam is reduced, the temperature of the hot water circulating in the sterilizing tank is reduced, and the temperature in the tank is reduced. Thus, a predetermined cooking and sterilizing temperature is maintained.
【0015】以上のように、熱交換器3の1次側に流入
する蒸気の温度をその入口で、過熱蒸気発生装置2によ
り再加熱して、熱交換器3に入る蒸気の温度を短時間で
上昇させ、追従して熱交換器3の2次側を循環し含気食
品に噴射される熱水の温度を上げることにより、槽内温
度と食品温度の立上りを早め、短時間で所定の温度時間
推移曲線に追従する制御を行うことができる。As described above, the temperature of the steam flowing into the primary side of the heat exchanger 3 is reheated at the inlet thereof by the superheated steam generator 2, and the temperature of the steam entering the heat exchanger 3 is reduced for a short time. And circulates the secondary side of the heat exchanger 3 to increase the temperature of the hot water injected into the aerated food, thereby accelerating the rise of the temperature in the tank and the temperature of the food. Control that follows the temperature-time transition curve can be performed.
【0016】図2は本発明の詳細を示す2段階昇温制御
による温度時間推移曲線、図3は3段階昇温による温度
時間推移曲線、図4は4段階昇温制御による温度時間推
移曲線を示し、横軸に時間Tを、縦軸に槽内温度t℃を
表示している。以下、この温度時間推移曲線に沿って殺
菌および調理システムの作用を説明する。図2におい
て、予め制御盤24には、これらの温度時間推移曲線に
沿った制御プログラムが入力されており、槽内温度セン
サ23、圧力センサ18および熱水温度センサ22の検
出値が制御盤24に集り、逐次制御プログラムに取り込
み、温度時間推移曲線に沿った槽内温度を追従するよう
に制御する。FIG. 2 is a temperature-time transition curve based on two-stage heating control showing details of the present invention, FIG. 3 is a temperature-time transition curve based on three-stage heating, and FIG. In the graph, the horizontal axis represents time T, and the vertical axis represents the tank temperature t ° C. Hereinafter, the operation of the sterilization and cooking system will be described along the temperature-time transition curve. In FIG. 2, control programs along these temperature-time transition curves are input to the control panel 24 in advance, and the detection values of the tank temperature sensor 23, the pressure sensor 18, and the hot water temperature sensor 22 are stored in the control panel 24. And sequentially incorporated in a control program to control the temperature in the bath along the temperature-time transition curve.
【0017】殺菌槽6に含気食品を収容し、制御盤24
によりこの殺菌および調理システムを起動し、蒸気調整
アナログ弁1を開き、ボイラーから加熱蒸気が過熱蒸気
発生装置2を通して熱交換器3に流入し、蒸気調整アナ
ログ弁1を調節して加熱蒸気の流量を増し、過熱蒸気発
生装置2により加熱蒸気の温度を上げて熱交換器3の1
次側に流し、循環ポンプ5により熱交換器3の2次側を
流れる熱水と熱交換して熱水の温度を上げ、殺菌槽6の
注水容器14から熱水を含気食品に噴射して加熱し、同
時に殺菌槽6の温度を上昇させる。The sterilized tank 6 contains the aerated food, and the control panel 24
To start the sterilization and cooking system, open the steam control analog valve 1, heat steam from the boiler flows into the heat exchanger 3 through the superheated steam generator 2, and adjust the steam control analog valve 1 to control the flow rate of the heat steam. And the temperature of the heated steam is increased by the superheated steam generator 2 to increase the temperature of the heat exchanger 3.
The hot water flows to the next side, exchanges heat with the hot water flowing on the secondary side of the heat exchanger 3 by the circulation pump 5, raises the temperature of the hot water, and injects hot water from the water injection container 14 of the sterilization tank 6 to the aerated food. To raise the temperature of the sterilization tank 6 at the same time.
【0018】この時、殺菌槽6内に設けた槽内温度セン
サ23および圧力センサ18により、槽内温度と槽内気
圧を検出し制御盤24に送り、槽内温度が所定温度(8
0〜100℃)に達するまで急速に加熱し(5〜15分
間)、殺菌槽6内の気圧をコンプレッサ16により槽内
温度に見合う気圧に維持する(1次昇温A区間)。槽内
温度が所定温度に達すると、熱水温度を熱水温度センサ
22により検出し、その熱水温度を維持するように蒸気
調整アナログ弁1と過熱蒸気発生装置2を調整し、食品
により異なる所定時間、含気食品の調理を行う(調理B
区間)。食品の中心部温度は、図中点線のように槽内温
度の変化に遅れて追従する。所定時間経過して含気食品
の調理が完了すると、蒸気調整アナログ弁1と過熱蒸気
発生装置2を操作して熱水の温度を上げ、槽内温度を所
定殺菌温度(110〜120℃)まで上げて、所定時間
(2〜10分)その状態を保持して殺菌を行い(殺菌C
区間)、以後急冷して含気食品を常温に戻す(冷却E区
間)。以上のように、槽内温度を温度時間推移曲線に沿
って制御することにより、比較的に低い温度で調理を行
い、殺菌処理は高い殺菌温度で短時間に処理することに
より、調理の進み過ぎを防止し確実な殺菌処理を行うこ
とができる。At this time, the inside temperature of the tank and the inside pressure of the tank are detected by the inside temperature sensor 23 and the inside pressure sensor 18 provided in the sterilization tank 6 and sent to the control panel 24, and the inside temperature of the tank is adjusted to a predetermined temperature (8
(0 to 100 ° C.), and rapidly heated (5 to 15 minutes) until the pressure in the sterilization tank 6 is maintained at a pressure corresponding to the temperature in the sterilization tank 6 by the compressor 16 (first temperature rise A section). When the temperature in the tank reaches a predetermined temperature, the hot water temperature is detected by the hot water temperature sensor 22, and the steam control analog valve 1 and the superheated steam generator 2 are adjusted so as to maintain the hot water temperature. Cooking of the aerated food for a predetermined time (cooking B
section). The temperature at the center of the food follows the change in the temperature in the tank with a delay, as indicated by the dotted line in the figure. When the cooking of the aerated food is completed after a predetermined time, the temperature of the hot water is increased by operating the steam control analog valve 1 and the superheated steam generator 2, and the temperature in the tank is reduced to a predetermined sterilization temperature (110 to 120 ° C). And sterilize while maintaining the state for a predetermined time (2 to 10 minutes) (sterilization C
Section), and then rapidly cooled to return the aerated food to normal temperature (Cooling E section). As described above, cooking is performed at a relatively low temperature by controlling the temperature in the bath along the temperature-time transition curve, and sterilization is performed at a high sterilization temperature in a short time, so that cooking proceeds excessively. And a reliable sterilization treatment can be performed.
【0019】図3においては、同様に殺菌槽6の槽内温
度が所定温度(80〜100℃)に達するまで急速に加
熱し(5〜15分間)、殺菌槽内の気圧をコンプレッサ
16により槽内温度に見合う気圧に維持する(1次昇温
A区間)。槽内温度が所定温度に達すると、熱水温度を
熱水温度センサ22により検出し、その熱水温度を維持
するように蒸気調整アナログ弁1と過熱蒸気発生装置2
を調整し、食品により定まる所定時間、含気食品の調理
を行う(調理B1区間)。ついで調理を促進させるため
に、槽内温度をさらに所定の追加調理および殺菌温度
(110〜120℃)まで上げ、所定時間(2〜10分
間)維持して調理を完了させるとともに殺菌処理を行う
(2次昇温B2区間)。含気食品が調理時間の異なる素
材の混合で構成されている場合には、この2次昇温によ
り短時間で確実な調理と殺菌処理を行うことができる。
調理が完了すると、槽内温度を所定殺菌温度(122〜
124℃)まで上げて、ほぼ1分間その状態を保持して
高温殺菌を行い(3次昇温C区間)、以後急冷して含気
食品を常温に戻す(冷却E区間)。In FIG. 3, the sterilizing tank 6 is heated rapidly (5 to 15 minutes) until the temperature in the sterilizing tank 6 reaches a predetermined temperature (80 to 100 ° C.). It is maintained at a pressure corresponding to the internal temperature (first temperature rise A section). When the temperature in the tank reaches a predetermined temperature, the hot water temperature is detected by the hot water temperature sensor 22 and the steam regulating analog valve 1 and the superheated steam generator 2 are maintained so as to maintain the hot water temperature.
Is adjusted, and the aerated food is cooked for a predetermined time determined by the food (cooking B1 section). Then, in order to promote the cooking, the temperature in the tank is further raised to a predetermined additional cooking and sterilization temperature (110 to 120 ° C.), and the cooking is completed while the predetermined time (2 to 10 minutes) is maintained, and the sterilization process is performed ( Secondary heating B2 section). When the aerated food is composed of a mixture of materials having different cooking times, reliable cooking and sterilization can be performed in a short time by this secondary heating.
When the cooking is completed, the temperature in the tank is set to a predetermined sterilization temperature (122 to
124 ° C.), hold the state for about 1 minute, and perform high-temperature sterilization (third temperature rising C section), and then rapidly cool the air-containing food to normal temperature (cooling E section).
【0020】図4においては、同様に殺菌槽6の槽内温
度が所定温度(80〜100℃)に達するまで急速に加
熱し(5〜15分間)、殺菌槽内の気圧をコンプレッサ
16により槽内温度に見合う気圧に維持する(1次昇温
A区間)。槽内温度が所定温度に達すると、熱水温度を
熱水温度センサ22により検出し、その熱水温度を維持
するように蒸気調整アナログ弁1と過熱蒸気発生装置2
を調整し、食品により定まる所定時間、含気食品の調理
を行う(調理B1区間)。ついで調理を促進させるため
に、槽内温度をさらに所定の追加調理および殺菌温度
(100〜110℃)まで上げ、所定時間(1〜4分
間)維持して調理を完了させるとともに殺菌処理を行う
(2次昇温B2区間)。調理が完了すると、槽内温度を
所定殺菌温度(120℃)まで上げて、所定時間(1〜
4分間)維持して殺菌を行う(3次昇温C区間)。さら
に、槽内温度を所定殺菌温度(122〜124℃)まで
上げて、ほぼ1分間その状態を保持して高温殺菌を行い
(4次昇温D区間)、以後急冷して含気食品を常温に戻
す(冷却E区間)。In FIG. 4, the sterilizing tank 6 is heated rapidly (5 to 15 minutes) until the temperature in the sterilizing tank 6 reaches a predetermined temperature (80 to 100 ° C.). It is maintained at a pressure corresponding to the internal temperature (first temperature rise A section). When the temperature in the tank reaches a predetermined temperature, the hot water temperature is detected by the hot water temperature sensor 22 and the steam regulating analog valve 1 and the superheated steam generator 2 are maintained so as to maintain the hot water temperature.
Is adjusted, and the aerated food is cooked for a predetermined time determined by the food (cooking B1 section). Then, in order to promote cooking, the temperature in the tank is further raised to a predetermined additional cooking and sterilization temperature (100 to 110 ° C.), and maintained for a predetermined time (1 to 4 minutes) to complete cooking and perform a sterilization process ( Secondary heating B2 section). When the cooking is completed, the temperature in the tank is raised to a predetermined sterilization temperature (120 ° C.), and the temperature is raised for a predetermined time (1 to 1).
(4 minutes) and sterilization is performed (third temperature rise C section). Furthermore, the temperature in the tank is raised to a predetermined sterilization temperature (122 to 124 ° C.), and the state is maintained for approximately one minute to perform high-temperature sterilization (fourth heating D section). (Cooling E section).
【0021】以上のように、半調理状態で封入された含
気食品を殺菌槽で調理を確実に完了させるともに、引き
続き槽内温度を上げて殺菌処理することにより、含気食
品が外気にさらされ酸化することなく調理することがで
き、調理温度から高温度に上げ、比較的短時間で殺菌処
理することができる。また、殺菌温度を高くし短時間で
殺菌処理することにより、短時間でF値4のの殺菌条件
を満足する殺菌処理を行うことができる。また、含気食
品が殺菌のため高温状態に置かれる時間を短くすること
ができ、含気食品の調理の進み過ぎ、袋また缶等の匂い
の付着を避けることができる。As described above, cooking of the aerated food enclosed in a semi-cooked state is surely completed in the sterilizing tank, and the aerated food is exposed to the outside air by successively increasing the temperature in the tank and sterilizing. It can be cooked without being oxidized, can be heated from a cooking temperature to a high temperature, and can be sterilized in a relatively short time. In addition, by performing the sterilization treatment in a short time by increasing the sterilization temperature, the sterilization treatment that satisfies the sterilization condition of the F value of 4 can be performed in a short time. In addition, the time during which the aerated food is kept in a high temperature state for sterilization can be shortened, and the cooking of the aerated food can be prevented from proceeding too much, and the smell of bags or cans can be prevented from adhering.
【0022】[0022]
【発明の効果】以上のように、本発明では、調理未完了
の食品を耐熱容器に充填し、殺菌槽に収容して加熱調理
し、調理完了したら温度を上げて引き続き殺菌処理する
ように食品の中心温度を多段階に制御することにより、
調理と殺菌処理を連続して行う。殺菌のため長時間に亘
って含気食品を高い温度にさらすことなく、食品の味や
匂いを損なったり、調理が過剰になる等の問題を避ける
ことができる。さらに、冷却水槽内で充分に冷却した冷
却水を殺菌槽に注水で、食品を急速に常温に下げること
ができ、長時間殺菌温度にさらすことによる食品の味や
匂いの低下を防げる。また、冷却に使用する冷却水は冷
却水槽を交互に使用することにより、回収し冷却水槽内
で充分に冷却し再使用できる。As described above, according to the present invention, uncooked food is filled in a heat-resistant container, stored in a sterilization tank, heated and cooked, and after cooking is completed, the food is heated and sterilized. By controlling the center temperature of the
Cooking and sterilization are performed continuously. It is possible to avoid problems such as impairing the taste and smell of food and excessive cooking without exposing the aerated food to high temperatures for a long period of time for sterilization. Further, by pouring cooling water sufficiently cooled in the cooling water tank into the sterilizing tank, the food can be rapidly cooled to room temperature, and the taste and smell of the food due to long-term exposure to the sterilizing temperature can be prevented. In addition, the cooling water used for cooling can be collected, cooled sufficiently in the cooling water tank, and reused by alternately using the cooling water tanks.
【図1】含気食品の殺菌および調理システムの構成を示
すブロック図である。FIG. 1 is a block diagram showing a configuration of a system for sterilizing and cooking aerated food.
【図2】本発明の詳細を示す2段階昇温による温度時間
推移曲線である。FIG. 2 is a temperature-time transition curve according to a two-stage temperature increase showing details of the present invention.
【図3】本発明の詳細を示す3段階昇温による温度時間
推移曲線である。FIG. 3 is a temperature-time transition curve based on a three-step temperature rise showing details of the present invention.
【図4】本発明の詳細を示す4段階昇温による温度時間
推移曲線である。FIG. 4 is a temperature-time transition curve by four-step temperature rise showing details of the present invention.
【図5】従来の殺菌および調理システムの詳細を示す温
度時間推移曲線である。FIG. 5 is a temperature-time curve showing details of a conventional sterilization and cooking system.
1 蒸気調整アナログ弁 2 過熱蒸気発生装置 3 熱交換器 4a 2方向切換弁 4b 2方向切換弁 5 循環ポンプ 6 殺菌槽 7 排水弁 8a 開閉弁 8b 開閉弁 8c 開閉弁 9 熱水回収タンク 10 第1冷却水槽 11 冷却水管路 12 第2冷却水槽 13 台車 14 注水容器 15 空気圧力管 16 コンプレッサ 17 圧力調整アナログ弁 18 圧力センサ 19 排気アナログ弁 20 供給管路 21 還流管路 22 熱水温度センサ 23 槽内温度センサ 24 制御盤 DESCRIPTION OF SYMBOLS 1 Steam control analog valve 2 Superheated steam generator 3 Heat exchanger 4a 2-way switching valve 4b 2-way switching valve 5 Circulation pump 6 Sterilization tank 7 Drain valve 8a Open / close valve 8b Open / close valve 8c Open / close valve 9 Hot water recovery tank 10 First Cooling water tank 11 Cooling water pipe 12 Second cooling water tank 13 Truck 14 Water injection container 15 Air pressure pipe 16 Compressor 17 Pressure control analog valve 18 Pressure sensor 19 Exhaust analog valve 20 Supply pipe 21 Reflux pipe 22 Hot water temperature sensor 23 Inside tank Temperature sensor 24 Control panel
Claims (3)
し、容器内を不活性ガス置換して密封した含気食品を殺
菌槽に収容し、この食品の中心温度を次の(1)乃至
(5)の工程順に多段階に変動することを特徴とする含
気食品の殺菌及び加熱調理法。 (1) 食品の中心温度を、5〜15分の間に80〜1
00℃まで急速に昇温する1次昇温工程、 (2) 前記80〜100℃までの食品の中心温度を、
含気食品の種類と量に基づく所定時間の間保持する調理
恒温工程、 (3) 食品の中心温度を、食品殺菌温度110〜12
0℃まで昇温する2次昇温工程、 (4) 前記110〜120℃までの食品の中心温度
を、2〜10分保持する殺菌処理工程、 (5) 冷却水槽を複数設け、該冷却水槽内の冷却水を
冷却し、該いずれか1つの冷却水槽内の冷却水を殺菌槽
内に注水して前記食品の中心温度を4〜15分で急速に
常温に下げた後、冷却に使用した冷却水を冷却水槽に回
収し冷却するとともに、次の冷却のときには前回と別の
冷却水槽内の冷却水を使用する冷却工程。A heat-resistant container is filled with uncooked food, and the inside of the container is replaced with an inert gas, and the sealed aerated food is stored in a sterilization tank. The center temperature of the food is determined by the following (1). A method of sterilizing and heating an aerated food, wherein the method varies in multiple stages in the order of steps (5) to (5). (1) Set the center temperature of the food to 80 to 1 in 5 to 15 minutes.
A primary temperature raising step of rapidly raising the temperature to 00 ° C., (2) the central temperature of the food to 80 to 100 ° C.,
A cooking constant temperature step of maintaining for a predetermined time based on the type and amount of the aerated food; (3) setting the central temperature of the food to a food sterilization temperature of 110 to 12;
A secondary temperature raising step of raising the temperature to 0 ° C., (4) a sterilizing step of maintaining the center temperature of the food to 110 to 120 ° C. for 2 to 10 minutes, (5) a plurality of cooling water tanks, The cooling water in the inside was cooled, the cooling water in any one of the cooling water tanks was poured into the sterilization tank, and the central temperature of the food was rapidly lowered to room temperature in 4 to 15 minutes, and then used for cooling. A cooling process in which cooling water is collected in a cooling water tank and cooled, and for the next cooling, cooling water in another cooling water tank is used.
容器内を不活性ガス置換して密封した含気食品を殺菌槽
に収容し、この食品の中心温度を次の(1)乃至(6)
の工程順に多段階に変動することを特徴とする含気食品
の殺菌および加熱調理法。 (1) 食品の中心温度を、5〜15分の間に80〜1
00℃まで急速に昇温する1次昇温工程、 (2) 前記80〜100℃までの食品の中心温度を、
含気食品の種類と量に基づく所定時間の間保持する調理
恒温工程、 (3) 食品の中心温度を、食品殺菌温度110〜12
0℃まで昇温する2次昇温工程、 (4) 前記110〜120℃までの食品の中心温度
を、2〜10分保持する殺菌処理工程、 (5) 前記食品の中心温度を、さらに122〜124
℃までに急速に上げ、ほぼ1分保持する高温殺菌処理工
程、 (6) 冷却水槽を複数設け、該冷却水槽内の冷却水を
冷却し、該いずれか1つの冷却水槽内の冷却水を殺菌槽
内に注水して前記122〜124℃の食品の中心温度を
4〜15分で急速に常温に下げた後、冷却に使用した冷
却水を当該冷却水槽に回収し冷却するとともに、次の冷
却のときには前回と別の冷却水槽内の冷却水を使用する
冷却工程。2. A heat-resistant container is filled with uncooked food,
The air-containing food sealed by replacing the inside of the container with an inert gas is accommodated in a sterilization tank, and the center temperature of the food is set in the following (1) to (6).
And sterilizing and heating the aerated food, wherein the method varies in multiple stages in the order of the steps. (1) Set the center temperature of the food to 80 to 1 in 5 to 15 minutes.
A primary temperature raising step of rapidly raising the temperature to 00 ° C., (2) the central temperature of the food to 80 to 100 ° C.,
A cooking constant temperature step of maintaining for a predetermined time based on the type and amount of the aerated food; (3) setting the central temperature of the food to a food sterilization temperature of 110 to 12;
(4) a sterilization process in which the center temperature of the food up to 110 to 120 ° C. is maintained for 2 to 10 minutes; and (5) a center temperature of the food in addition to 122. ~ 124
(C) A plurality of cooling water tanks are provided, the cooling water in the cooling water tank is cooled, and the cooling water in one of the cooling water tanks is sterilized. After pouring water into the tank and rapidly lowering the central temperature of the food at 122 to 124 ° C. to normal temperature in 4 to 15 minutes, the cooling water used for cooling is collected in the cooling water tank and cooled, and the next cooling is performed. In this case, a cooling process using cooling water in a different cooling water tank from the previous time.
容器内を不活性ガス置換して密封した含気食品を殺菌槽
に収容し、この食品の中心温度を次の(1)乃至(7)
の工程順に多段階に変動することを特徴とする含気食品
の殺菌および加熱調理法。 (1) 食品の中心温度を、5〜15分の間に80〜1
00℃まで急速に昇温する1次昇温工程、 (2) 前記80〜100℃までの食品の中心温度を、
含気食品の種類と量に基づく所定時間の間保持する調理
恒温工程、 (3) 食品の中心温度を、3〜4分の間にほぼ110
℃まで急速に昇温する追加調理工程、 (4) 食品の中心温度を、食品殺菌温度120℃まで
昇温する2次昇温工程、 (5) 前記食品の中心温度を、3〜4分保持する殺菌
処理工程、 (6) 前記食品の中心温度を、さらに122〜124
℃に急速に上げ、ほぼ1分保持する高温殺菌処理工程、 (7) 冷却水槽を複数設け、該冷却水槽内の冷却水を
冷却し、該いずれか1つの冷却水槽内の冷却水を殺菌槽
内に注水して前記食品の中心温度を4〜15分で急速に
常温に下げた後、冷却に使用した冷却水を冷却水槽に回
収し冷却するとともに、次の冷却のときには前回と別の
冷却水槽内の冷却水を使用する冷却工程。3. Filling the heat-resistant container with uncooked food,
The aerated food sealed by replacing the inside of the container with an inert gas is accommodated in a sterilization tank, and the center temperature of the food is determined by the following (1) to (7).
And sterilizing and heating the aerated food, wherein the method varies in multiple stages in the order of the steps. (1) Set the center temperature of the food to 80 to 1 in 5 to 15 minutes.
A primary temperature raising step of rapidly raising the temperature to 00 ° C., (2) the central temperature of the food to 80 to 100 ° C.,
(3) keeping the center temperature of the food at about 110 in 3 to 4 minutes, wherein the cooking temperature is maintained for a predetermined time based on the type and amount of the aerated food;
Additional cooking step of rapidly raising the temperature to 0 ° C., (4) secondary temperature raising step of raising the central temperature of the food to the food sterilization temperature of 120 ° C., (5) maintaining the central temperature of the food for 3 to 4 minutes (6) The central temperature of the food is further increased by 122 to 124.
° C, and a high-temperature sterilization treatment step of rapidly raising the temperature to about 1 minute, and (7) providing a plurality of cooling water tanks, cooling the cooling water in the cooling water tank, and dissolving the cooling water in any one of the cooling water tanks After the water is poured into the chiller and the center temperature of the food is rapidly lowered to room temperature in 4 to 15 minutes, the cooling water used for cooling is collected in a cooling water tank and cooled, and the next cooling is different from the previous cooling. Cooling process using cooling water in the water tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6131398A JP3053529B2 (en) | 1994-05-20 | 1994-05-20 | Sterilization and cooking of aerated foods |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6131398A JP3053529B2 (en) | 1994-05-20 | 1994-05-20 | Sterilization and cooking of aerated foods |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07313125A JPH07313125A (en) | 1995-12-05 |
JP3053529B2 true JP3053529B2 (en) | 2000-06-19 |
Family
ID=15057048
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP6131398A Expired - Fee Related JP3053529B2 (en) | 1994-05-20 | 1994-05-20 | Sterilization and cooking of aerated foods |
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JP (1) | JP3053529B2 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
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JP3342872B2 (en) * | 1994-03-04 | 2002-11-11 | 小野食品興業株式会社 | Pneumatic cooking system |
JP4733467B2 (en) * | 2004-11-10 | 2011-07-27 | ハウス食品株式会社 | Retort container manufacturing method |
JP2007159517A (en) * | 2005-12-16 | 2007-06-28 | Samson Co Ltd | Heat sterilization apparatus |
BRPI0801053A2 (en) * | 2008-02-11 | 2009-11-17 | Pascoal Sante Caruso | food production and preservation process valid for up to four years |
JP5340805B2 (en) * | 2009-05-20 | 2013-11-13 | アルファフーズ株式会社 | Bag-packed livestock sausage and method for producing the same |
JP5531519B2 (en) * | 2009-09-08 | 2014-06-25 | 東洋製罐株式会社 | Batch retort sterilization method and apparatus |
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Publication number | Priority date | Publication date | Assignee | Title |
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JPS5266643A (en) * | 1975-11-29 | 1977-06-02 | Fujimori Kogyo Co | Heat sterilizing method of packed food |
JP2994399B2 (en) * | 1989-03-28 | 1999-12-27 | 大日本印刷株式会社 | Retort processing method of corn with shaft |
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1994
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JPH07313125A (en) | 1995-12-05 |
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