JPH0126669B2 - - Google Patents
Info
- Publication number
- JPH0126669B2 JPH0126669B2 JP12650384A JP12650384A JPH0126669B2 JP H0126669 B2 JPH0126669 B2 JP H0126669B2 JP 12650384 A JP12650384 A JP 12650384A JP 12650384 A JP12650384 A JP 12650384A JP H0126669 B2 JPH0126669 B2 JP H0126669B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- retort
- old
- cooling
- temperature
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 57
- 238000001816 cooling Methods 0.000 claims description 19
- 230000001954 sterilising effect Effects 0.000 claims description 16
- 238000004659 sterilization and disinfection Methods 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 14
- 235000013324 preserved food Nutrition 0.000 claims description 14
- 239000013505 freshwater Substances 0.000 description 19
- 239000000498 cooling water Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 3
- 239000003673 groundwater Substances 0.000 description 3
- 239000008399 tap water Substances 0.000 description 3
- 235000020679 tap water Nutrition 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
Landscapes
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明はレトルト殺菌処理法に関し、さらに詳
しくはコーヒ缶詰等の缶詰のバツチ式蒸気レトル
ト殺菌処理法に関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a retort sterilization method, and more particularly to a batch-type steam retort sterilization method for canned goods such as canned coffee.
(従来の技術)
従来缶詰をバツチ式レトルトで蒸気加熱殺菌処
理する場合、殺菌温度(例えば120℃)での殺菌
工程が終了した後、レトルト内に新水である水道
水又は地下水等(通常25℃以下)の冷却水をほぼ
満水になるまで給水し、缶詰の温度がほぼ40℃
(通常35〜42℃)になるまで冷却した後、缶詰を
レトルトより送出するプロセスをとつている。(Prior art) When conventionally canned food is sterilized by steam heating in a batch-type retort, after the sterilization process at the sterilization temperature (for example, 120°C) is completed, fresh water such as tap water or ground water (usually 25°C) is poured into the retort. ℃ or below) until the water is almost full, and the temperature of the canned food is approximately 40℃.
After cooling the canned food to a temperature of 35 to 42 degrees Celsius (usually 35 to 42 degrees Celsius), the canned food is sent out from a retort.
この冷却のさい、冷却水の温度が上昇するの
で、レトルトが大容量(例えば約10〜20トン)
で、収容される缶詰の量が多い場合、1回のほぼ
満水になるまでの新水の給水では、40℃近傍まで
缶詰を冷却することが困難で、例えば約60℃で缶
詰と冷却水の温度がほぼ平衡状態となる。そのた
め、このほぼ平衡状態に達した後、ほぼ満水状態
を保持するよう冷却水をオーバフローさせなが
ら、新水をレトルト内に補給して、缶詰をほぼ40
℃まで冷却していた。 During this cooling, the temperature of the cooling water increases, so the retort has a large capacity (for example, about 10 to 20 tons).
If there are a large number of canned goods to be stored, it is difficult to cool the canned goods to around 40℃ by supplying fresh water until the water is almost full at once. The temperature is almost at equilibrium. Therefore, after reaching this almost equilibrium state, fresh water is replenished into the retort while overflowing the cooling water to maintain the almost full water state, and the canned food is kept for about 40 minutes.
It was cooled down to ℃.
缶詰をレトルト内でほぼ40℃(35〜42℃)まで
冷却するのは、この温度が、室温保存中に細菌の
復活が起らない上限であるからである。また缶詰
をこの温度範囲を越えてさらに低い温度まで冷却
すると、処理時間が徒らに永びくのみならず、夏
期湿度の高い時などには、缶詰表面に結露を生ず
る等の好ましくない現象が起り易いからである。 Canned food is cooled in the retort to approximately 40°C (35-42°C) because this temperature is the upper limit at which bacterial resurgence does not occur during room temperature storage. Furthermore, if canned goods are cooled to a lower temperature than this temperature range, not only will the processing time be unnecessarily prolonged, but also undesirable phenomena such as condensation forming on the surface of the canned goods may occur during high humidity in the summer. This is because it is easy.
(発明が解決しようとしている問題点)
以上のように、1回の殺菌処理に対して、オー
バフローさせながら新水をレトルト内に補給する
ことは、特にレトルトが大容量の場合、多量の新
水を使用することになり、新水が水道水の場合は
水コストの上昇を招き、地下水の場合は汲上規制
に抵触するおそれを生じ易く、また何れの場合も
排水料が高くなるという問題を生ずる。(Problem to be solved by the invention) As described above, replenishing fresh water into the retort while overflowing for one sterilization treatment requires a large amount of fresh water, especially when the retort has a large capacity. If the new water is tap water, this will lead to an increase in water costs, and if the new water is groundwater, there is a risk of violating pumping regulations, and in both cases, there will be problems such as higher drainage fees. .
(発明の目的)
本発明は以上に述べた従来技術の問題点に鑑み
なされたものであつて、本発明の目的は、冷却水
としての新水の使用量が節減できる、特に大容量
のバツチ式レトルトに適した、蒸気レトルト殺菌
処理法を提供することにある。(Object of the Invention) The present invention has been made in view of the problems of the prior art described above, and an object of the present invention is to reduce the amount of fresh water used as cooling water, and to reduce the amount of fresh water used as cooling water. An object of the present invention is to provide a steam retort sterilization method suitable for type retorts.
(発明の構成)
上記目的を達成するため、本発明は殺菌工程終
了後、旧水タンクより旧水をレトルト内にほぼ満
水になるまで給水して、缶詰と旧水の温度がほぼ
平衡状態に達するまで該缶詰を1次冷却した後、
該旧水を該レトルトより排出し、直ちに25℃以下
の新水を該レトルト内にほぼ満水になるまで給水
して、該缶詰の温度をほぼ40℃まで2次冷却し、
次いで該新水を該レトルトより排出して、該旧水
タンクに送入し、旧水として、次の殺菌工程後の
1次冷却に使用することを特徴とする缶詰の蒸気
レトルト殺菌処理法を提供するものである。(Structure of the Invention) In order to achieve the above object, the present invention supplies old water from the old water tank to the retort until it is almost full after the sterilization process is completed, so that the temperature of the canned food and the old water is almost in equilibrium. After first cooling the canned food until it reaches
Draining the old water from the retort, immediately supplying new water at 25°C or lower until the retort is almost full, and secondary cooling the canned food to approximately 40°C;
A steam retort sterilization method for canned goods, characterized in that the new water is then discharged from the retort, fed into the old water tank, and used as old water for primary cooling after the next sterilization step. This is what we provide.
(実施例)
以下図面を参照しながら本発明について説明す
る。(Example) The present invention will be described below with reference to the drawings.
第1図において、1は大容量の(通常約10〜20
トン)の横型バツチ式レトルトであり、レトルト
1には、仕切り板2を介して、バスケツト3に積
載された多数の缶詰4が収容され、冷却水5がほ
ぼ満水となるまで給水されている。6は新水タン
クであり、水源7より、地下水又は水道水の新水
が供給される。新水の温度は、缶詰の温度を数分
のオーダの短時間に、ほぼ40℃(35〜42℃)に2
次冷却するために、25℃以下であることが望まし
い。この点で年間を通じて約10〜20℃の水温が安
定して得られる地下水を新水として用いることが
好ましい。新水はポンプ8およびバルブ9を介し
て、上部からレトルト1に給水される。 In Figure 1, 1 indicates a large capacity (usually about 10 to 20
The retort 1 is a horizontal batch type retort with a capacity of 1.5 tons, and a large number of canned goods 4 loaded in a basket 3 are accommodated in the retort 1 via a partition plate 2, and cooling water 5 is supplied until it is almost full. 6 is a fresh water tank, and fresh water such as underground water or tap water is supplied from a water source 7. The temperature of the new water can be reduced to approximately 40°C (35-42°C) in a short period of time, on the order of a few minutes.
For subsequent cooling, it is desirable to be below 25°C. In this respect, it is preferable to use groundwater as the fresh water, which can stably maintain a water temperature of about 10 to 20°C throughout the year. Fresh water is supplied to the retort 1 from above via a pump 8 and a valve 9.
10は旧水タンクである。本明細書において旧
水とは、新水がレトルト1内で缶詰4の2次冷却
に一たん使用された後、旧水タンク10に送られ
たものを称する。旧水の温度は、通常約40℃以下
である。缶詰4の2次冷却が終了した後、冷却水
5(新水)はポンプ11およびバルブ12を介し
て、旧水タンク10に送られて、旧水として一時
貯留される。缶詰4の1次冷却にさいしては、旧
水はポンプ13およびバルブ14を介して、上部
よりレトルト1内に給水される。1次冷却の終了
した旧水は、ポンプ11、バルブ15を介して排
水タンク16に導かれ、バルブ17を介して外部
に排出される。なお18は蒸気弁である。 10 is an old water tank. In this specification, old water refers to fresh water that is sent to the old water tank 10 after being used for secondary cooling of the canned goods 4 in the retort 1. The temperature of the old water is usually below about 40°C. After the secondary cooling of the cans 4 is completed, the cooling water 5 (new water) is sent to the old water tank 10 via the pump 11 and the valve 12, and is temporarily stored as old water. For the primary cooling of the cans 4, old water is supplied into the retort 1 from above via the pump 13 and valve 14. The old water that has undergone primary cooling is led to a drainage tank 16 via a pump 11 and a valve 15, and is discharged to the outside via a valve 17. Note that 18 is a steam valve.
(作用)
第2図は以上の冷却システムを備えた、内容積
20m3の横型バツチ式レトルト1に、コーヒ缶詰4
(1個容量250グラム)を、約5千個収納したバス
ケツト3を5個収容して、レトルト蒸気殺菌処理
した場合の、加熱冷却線図の例を示したものであ
る。なお温度は缶詰内の温度を示す。(Function) Figure 2 shows the internal volume of the system equipped with the above cooling system.
1 horizontal batch type retort of 20 m 3 , 4 canned coffee
This figure shows an example of a heating/cooling diagram when 5 baskets 3 containing about 5,000 baskets (each having a capacity of 250 grams) are stored and subjected to retort steam sterilization treatment. Note that the temperature indicates the temperature inside the can.
すなわちレトルト1内にバスケツト3を収容し
た後、密閉し、蒸気弁18を開くと、蒸気により
缶詰4は加熱され、約13分で120℃に達し、120〜
123℃で20分間殺菌処理(時間a―b)される。
直ちに蒸気弁18を閉じ、バルブ14を開いて、
旧水タンク10より例えば約37℃の旧水を、ほぼ
満水になるまでレトルト1内に1次給水する(時
間b―c)。この1次給水中およびほぼ満水後の
1次冷却期間(時間c―d)中に、缶詰4の温度
は低下し、一方旧水の温度は上昇し、この場合約
65℃において、両者はほぼ平衡状態に達する。 That is, after placing the basket 3 in the retort 1, sealing it and opening the steam valve 18, the canned food 4 is heated by the steam, reaching 120°C in about 13 minutes, and reaching 120°C.
Sterilize at 123°C for 20 minutes (times a-b).
Immediately close the steam valve 18 and open the valve 14,
For example, old water at about 37° C. is primarily supplied from the old water tank 10 into the retort 1 until it is almost full (time b-c). During this primary water supply and the primary cooling period (time c-d) after almost full water, the temperature of the canned food 4 decreases, while the temperature of the old water increases, in this case approximately
At 65°C, both reach an almost equilibrium state.
直ちにバルブ15を開いて、昇温した旧水を排
水タンク16に送出して(時間d―e)、1次排
水を行なう。 Immediately, the valve 15 is opened to send the heated old water to the drainage tank 16 (time de) to perform primary drainage.
1次排水終了後直ちに、バルブ9を開いて、新
水タンク6より、例えば20℃の新水をレトルト1
内にほぼ満水になるまで給水して、2次給水を行
なう(時間e―f)。この2次給水中およびほぼ
満水後の2次冷却期間(時間f―g)中に、缶詰
4の温度は、図の場合38℃まで低下し、新水の温
度もほぼこの温度まで上昇する。直ちに弁12を
開いて、加温され使用済の新水を、旧水として旧
水タンク10に送出して(時間g―h)、2次排
水を行なう。こ旧水タンク10内の旧水は、次の
回の殺菌後の1次冷却に再使用される。上記2次
排水後、レトルト1のドア(図示されない)を開
いて、殺菌冷却された缶詰4を、レトルト1から
送出する。 Immediately after the primary drainage is completed, open the valve 9 and pour fresh water at, for example, 20°C into the retort 1 from the fresh water tank 6.
Water is supplied until the tank is almost full, and secondary water supply is performed (times e-f). During this secondary water supply and the secondary cooling period (time fg) after the water is almost full, the temperature of the canned food 4 drops to 38°C in the case shown in the figure, and the temperature of the new water also rises to about this temperature. The valve 12 is immediately opened and the heated and used new water is sent to the old water tank 10 as old water (time gh) to perform secondary drainage. The old water in the old water tank 10 is reused for primary cooling after the next sterilization. After the secondary drainage, the door (not shown) of the retort 1 is opened, and the sterilized and cooled canned goods 4 are sent out from the retort 1.
以上の例の場合、従来のオーバフロー方式では
16トンの新水を必要としたのが、本発明の方式で
は、新水の給水量は12トンであつた。すなわちオ
ーバーフローされる新水の量が節減できる。また
新水と旧水の温度差は殺菌温度に比べて小さいの
で、旧水を用いたために冷却時間が永びくことは
ない。 In the above example, the conventional overflow method
Although 16 tons of fresh water was required, in the method of the present invention, the amount of fresh water supplied was 12 tons. In other words, the amount of fresh water that is overflowed can be reduced. Furthermore, since the temperature difference between the new water and the old water is smaller than the sterilization temperature, the cooling time will not be prolonged due to the use of the old water.
(発明の効果)
本発明によれば、殺菌工程終了後のレトルト内
冷却に使用される新水の量が節減できるという効
果を奏する。この節減のメリツトはレトルトが大
容量になるほど大きい。(Effects of the Invention) According to the present invention, it is possible to reduce the amount of fresh water used for cooling the inside of the retort after the sterilization process is completed. The benefits of this savings are greater as the capacity of the retort increases.
第1図は本発明の方法の実施に用られる装置の
例を示す説明図、第2図は本発明の方法を実施し
た場合における、缶詰内温度と時間との関係を示
す線図である。
1…レトルト、4…缶詰、6…新水タンク、1
0…旧水タンク。
FIG. 1 is an explanatory diagram showing an example of an apparatus used to carry out the method of the present invention, and FIG. 2 is a diagram showing the relationship between the internal temperature of a can and time when the method of the present invention is carried out. 1... Retort, 4... Canned food, 6... Fresh water tank, 1
0...Old water tank.
Claims (1)
ルト内にほぼ満水になるまで給水して、缶詰と旧
水の温度がほぼ平衡状態に達するまで該缶詰を1
次冷却した後、該旧水を該レトルトより排出し、
直ちに25℃以下の新水を該レトルト内にほぼ満水
になるまで給水して、該缶詰の温度をほぼ40℃ま
で2次冷却し、次いで該新水を該レトルトより排
出して、該旧水タンクに送入し、旧水として、次
の殺菌工程後の1次冷却に使用することを特徴と
する缶詰の蒸気レトルト殺菌処理法。1. After the sterilization process is completed, feed old water from the old water tank into the retort until it is almost full, and then store the canned goods for 1 hour until the temperature of the canned goods and the old water reach an almost equilibrium state.
After cooling, the old water is discharged from the retort,
Immediately feed new water at 25°C or below into the retort until it is almost full, cool the canned food secondary to approximately 40°C, then drain the new water from the retort and replace the old water with water. A steam retort sterilization method for canned goods, characterized in that the water is sent to a tank and used as old water for primary cooling after the next sterilization process.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12650384A JPS619273A (en) | 1984-06-21 | 1984-06-21 | Method for retort sterilization treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12650384A JPS619273A (en) | 1984-06-21 | 1984-06-21 | Method for retort sterilization treatment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS619273A JPS619273A (en) | 1986-01-16 |
| JPH0126669B2 true JPH0126669B2 (en) | 1989-05-24 |
Family
ID=14936817
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12650384A Granted JPS619273A (en) | 1984-06-21 | 1984-06-21 | Method for retort sterilization treatment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS619273A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01228448A (en) * | 1988-03-08 | 1989-09-12 | Fuji Seikan Kk | Two-step shower cooling process for high-temperature-sterilized packaged food and shower-producing unit |
| JP2012191910A (en) * | 2011-03-17 | 2012-10-11 | Tokyo Electric Power Co Inc:The | Sterilization system |
| CN121752124A (en) * | 2023-09-26 | 2026-03-27 | 株式会社日阪制作所 | Heating sterilization device, objects to be sterilized, and heating sterilization method |
| WO2025070307A1 (en) * | 2023-09-26 | 2025-04-03 | 株式会社日阪製作所 | Heat sterilization device, sterilization object, and heat sterilization method |
-
1984
- 1984-06-21 JP JP12650384A patent/JPS619273A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS619273A (en) | 1986-01-16 |
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