JP2598874B2 - Improved method of sterilizing canned foods with a sterilizing pot - Google Patents
Improved method of sterilizing canned foods with a sterilizing potInfo
- Publication number
- JP2598874B2 JP2598874B2 JP5259276A JP25927693A JP2598874B2 JP 2598874 B2 JP2598874 B2 JP 2598874B2 JP 5259276 A JP5259276 A JP 5259276A JP 25927693 A JP25927693 A JP 25927693A JP 2598874 B2 JP2598874 B2 JP 2598874B2
- Authority
- JP
- Japan
- Prior art keywords
- pot
- kettle
- hot water
- sterilization
- sterilizing
- 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 - Lifetime
Links
- 230000001954 sterilising effect Effects 0.000 title claims description 79
- 238000000034 method Methods 0.000 title claims description 25
- 235000013324 preserved food Nutrition 0.000 title claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 66
- 238000004659 sterilization and disinfection Methods 0.000 claims description 55
- 239000000498 cooling water Substances 0.000 claims description 10
- 238000001816 cooling Methods 0.000 description 6
- 238000011084 recovery Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 238000007599 discharging Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 101100298222 Caenorhabditis elegans pot-1 gene Proteins 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000009924 canning Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 235000013616 tea Nutrition 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/85—Food storage or conservation, e.g. cooling or drying
Landscapes
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は缶詰食品の殺菌方法、特
に殺菌釜による缶詰食品に殺菌を行う方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for sterilizing canned foods, and more particularly to a method for sterilizing canned foods in a sterilizing pot.
【0002】[0002]
【従来の技術】現在国内における缶詰食品の殺菌は、殆
ど伝統的な蒸気排気による殺菌方式であり、先ず蒸気で
殺菌釜内の空気をその釜内含有量がある程度低くなるま
で排除し、釜内温度が均一になってから、続けて蒸気を
導入し、釜内温度を殺菌温度まで上げて殺菌を行う。殺
菌完了後、需要により加圧冷却又は直接冷水で冷却を行
う。2. Description of the Related Art At present, sterilization of canned foods in Japan is almost a conventional sterilization method using steam exhaustion. First, air in a sterilization pot is removed by steam until the content in the pot is reduced to some extent. After the temperature becomes uniform, steam is continuously introduced, and the temperature in the pot is raised to the sterilization temperature to perform sterilization. After sterilization is completed, cooling is performed by pressurized cooling or direct cold water according to demand.
【0003】食品研究所王 家仁(1981年227号
研究報告)によると、蒸気排気方式による伝統的殺菌方
法のエネルギー消耗は殆ど排気段階に集中していて、釜
外に逃げる蒸気は使用される全部の蒸気の約三分の一を
占め、伝統的殺菌法のエネルギー使用効率を向上させる
必要がある。又、殺菌完了後の釜内高温蒸気は直接大気
中に排出され回収されていなく、高温釜体と釜内缶詰の
熱エネルギーも冷却水に持っていかれ回収されていない
ので、いずれも伝統的殺菌法のエネルギー使用効率不良
の問題を更に厳重にさせている。According to the Food Research Institute, Jinji Wang (Research Report No. 227, 1981), the energy consumption of the traditional sterilization method using the steam exhaust system is mostly concentrated in the exhaust stage, and steam that escapes from the pot is used. About one-third of the total steam needs to be used to improve the energy use efficiency of traditional sterilization methods. In addition, the high-temperature steam in the pot after the sterilization is completed is not directly discharged into the atmosphere and collected, and the heat energy of the high-temperature pot and the can in the pot is also taken and collected by the cooling water. The problem of inefficient use of energy by the law is becoming more severe.
【0004】本発明の主な目的は、殺菌釜による殺菌方
法に対するエネルギー効率の改良を提供する。[0004] The main object of the present invention is to provide an improvement in energy efficiency for a sterilization method using a sterilization pot.
【0005】[0005]
【発明の要旨】上記本発明の目的を達する為、下記特徴
を含む殺菌釜による缶詰食品に殺菌を行う改良方法を開
示した: (a)殺菌すべき缶詰を予め入れている殺菌釜に第一タ
ンクから約95℃の熱湯を導入し、殺菌釜が満水するま
で導入れた熱湯により釜内の空気を釜頂から排出させ、
該約95℃の熱湯は缶詰と釜体を予熱することにより約
85℃に低下することと、(b)該釜内の約85℃の熱
湯が釜内に無くなるまで殺菌釜の釜底から第二タンクに
流出させ、該流出の開始と共に該殺菌釜の頂部から蒸気
を導入し、導入した蒸気量は釜内正圧を保持するに充分
であり、空気は釜内に入らないことと、(c)該殺菌釜
内の温度が予定の殺菌温度に達するまで蒸気導入を続
け、該温度を予定の殺菌時間維持した後、蒸気導入を中
止することと、(d)該第二タンクの約85℃の熱湯を
殺菌釜に導入すると共に、釜頂から吹き撒き、該導入さ
れた約85℃の熱湯は釜内の蒸気を冷却し、高温釜体及
び釜内缶詰と熱交換を行い、約95℃に加熱され、一段
の時間を経た後、該殺菌釜内で約95℃に加熱された熱
湯を釜底から流出し始め、第一タンクに導入させ、該約
85℃の熱湯が殺菌釜に導入される量を(a)の約95
℃の熱湯を該殺菌釜に導入する量と略同じにすること
と、(e)上記(d)にて95℃に加熱された熱湯の流
出し完了後、該殺菌釜に冷却水を導入し始め、釜内の缶
詰に冷却を行ってから、冷却された殺菌缶詰食品を釜内
より取り出す。SUMMARY OF THE INVENTION To achieve the above objects of the present invention, there has been disclosed an improved method for sterilizing canned foods in a sterilizing kettle comprising the following features: About 95 ° C hot water is introduced from the tank, and the air in the kettle is discharged from the top of the pot with the hot water introduced until the sterilizing pot is full,
The hot water of about 95 ° C. is reduced to about 85 ° C. by preheating the can and the pot, and (b) the hot water of about 85 ° C. is removed from the bottom of the pot until the hot water at about 85 ° C. is no longer in the pot. Two tanks, steam is introduced from the top of the sterilization kettle at the start of the outflow, and the amount of introduced steam is sufficient to maintain a positive pressure in the kettle, and that air does not enter the kettle; c) steam introduction is continued until the temperature in the sterilization pot reaches a predetermined sterilization temperature, and after maintaining the temperature at a predetermined sterilization time, the steam introduction is stopped; and ℃ hot water is introduced into the sterilization pot and sprayed from the top of the pot, and the introduced hot water of about 85 ° C. cools the steam in the pot and exchanges heat with the high temperature pot and the can in the pot. ℃, and after a period of time, the hot water heated to about 95 ℃ in the sterilization pot flows out from the bottom of the pot Because, is introduced into the first tank, about the amount of hot water is introduced into the sterilization kettle 該約 85 ° C. of (a) 95
(E) After the hot water heated to 95 ° C. in the above (d) is drained, cooling water is introduced into the sterilizing pot. First, after cooling the cans in the pot, the cooled sterilized canned food is taken out from the pot.
【0006】上記本発明の方法において、温度が約95
℃の熱湯の好ましい温度は93−97℃の熱湯であり、
温度が約85℃の熱湯の好ましい温度は83−87℃の
熱湯である。In the method of the present invention, the temperature is about 95%.
The preferred temperature of hot water at ℃ is 93-97 ° C hot water,
A preferred temperature for hot water at a temperature of about 85 ° C is hot water at 83-87 ° C.
【0007】上記本発明の方法は、蒸気排気方式による
伝統的殺菌方法に較べ、下記の原因によりエネルギー効
率が顕著に向上される: 工程(a)にて、約95℃の熱湯で釜内の空気を排除
する方式により伝統的な蒸気で空気を釜外に排出する方
式を変えることで蒸気の使用を節約する。 工程(d)にて、約85℃の熱湯により殺菌完了後の
釜内の高温蒸気及び缶詰・釜体の熱エネルギーを回収す
る。The method of the present invention has a remarkable improvement in energy efficiency as compared with a traditional sterilization method using a steam exhaust system due to the following reasons: In step (a), hot water at about 95 ° C. The use of steam is saved by changing the method of discharging air outside the kettle with traditional steam by the method of eliminating air. In the step (d), high-temperature steam in the pot after completion of sterilization with hot water of about 85 ° C. and heat energy of the canned pot are recovered.
【0008】その他、高温殺菌釜の大部分の熱エネルギ
ーは有効に回収されるので、釜内温度は低下し、連帯的
に工程(e)に使われる冷却水量は伝統的な方法に使わ
れる冷却水量より少なくて済む。In addition, since most of the heat energy in the high-temperature sterilization pot is effectively recovered, the temperature in the pot is lowered, and the amount of cooling water used jointly in the step (e) is the cooling water used in the traditional method. It requires less than the amount of water.
【0009】[0009]
【発明の好ましい具体的実施方式の説明】図1は本発明
の殺菌方法の好ましい具体的実施方式のフローチャート
であり、それには本発明の方法を簡単明瞭に説明する
為、異なる段階の同じ殺菌釜をそれぞれ描いた。図1に
示す通り、本発明の好ましい具体的実施方法には、排気
段階、排水昇温段階、殺菌段階、熱回収段階及び冷却段
階の順序に5段階を含む。DESCRIPTION OF THE PREFERRED EMBODIMENTS OF THE INVENTION FIG. 1 is a flow chart of a preferred embodiment of the sterilization method of the present invention. I drew each. As shown in FIG. 1, the preferred embodiment of the present invention includes five steps in the order of the exhausting step, the drainage heating step, the sterilizing step, the heat recovery step and the cooling step.
【0010】排気段階において、約95℃の熱湯を第一
タンク10からポンプ11を経て、殺菌すべき缶詰を予
め入れている殺菌釜100に満水位まで注入する。殺菌
釜頂に設置されてる排気弁(図示してない)は既に予め
開いているので、釜内の空気は流入した熱湯により釜頂
の排気弁より排出されると共に、缶詰と釜体は予熱さ
れ、水温も約85℃まで低下する。In the evacuation stage, hot water of about 95 ° C. is injected from the first tank 10 via the pump 11 to the sterilization pot 100 in which cans to be sterilized are previously placed, to the full water level. Since the exhaust valve (not shown) installed at the top of the sterilization pot has already been opened beforehand, the air in the pot is discharged from the exhaust valve at the top of the pot by the flowing hot water, and the can and the pot are preheated. The water temperature also drops to about 85 ° C.
【0011】該排気段階に継ぐ排水昇温段階にて、該殺
菌釜100の釜底から釜内の熱湯を放出し第二タンク2
0に蓄えられ、釜内が無水になると水を放出する制御弁
を閉める、該放流開始と同時に該殺菌釜頂部より蒸気を
導入する、その量は釜内の蒸気圧を外界の圧力より大き
くするに充分であり、該第二タンク20内に放流した水
の温度は約85℃である。[0011] In the drainage temperature raising step following the exhausting step, the hot water in the pot is discharged from the pot bottom of the sterilization pot 100 and the second tank 2 is discharged.
Closed the control valve that releases water when the inside of the kettle becomes water-free, and introduces steam from the top of the sterilizing kettle simultaneously with the start of the discharge, the amount of which makes the steam pressure in the kettle higher than the external pressure The temperature of the water discharged into the second tank 20 is about 85 ° C.
【0012】排水昇温段階完了後、蒸気を釜底から導入
し、釜内の温度を続けて殺菌温度まで上昇させ、該温度
を指定の殺菌時間維持し、この段階にて、釜底に凝縮水
が蓄積していたら、釜底の排水弁を開き該凝縮水を排除
する。After completion of the drainage heating step, steam is introduced from the bottom of the pot, the temperature in the pot is continuously raised to the sterilization temperature, and the temperature is maintained for the specified sterilization time. If water has accumulated, open the drain valve at the bottom of the kettle to remove the condensed water.
【0013】殺菌段階完了後、熱回収段階を行うが、先
ず第二タンク20に蓄えてる約85℃の熱湯を、ポンプ
21の作用により殺菌釜100に送り釜頂から吹き撒
く。これで釜内の蒸気を凝縮しながら、殺菌温度にある
缶詰を均等に段々冷却させ、缶詰内外の圧力差を最小に
減少でき、圧縮空気を入れて釜圧を保持する必要がな
く、空気を圧縮に使う電気エネルギーも節約できる。8
5℃熱湯で熱交換を行い、熱エネルギーを回収する際、
95℃に加熱された熱湯が釜内に相当容量蓄積したら、
釜底から放流し始め、第一タンク10に導入し、熱湯が
釜を進出につやす時間を節約できる。該殺菌釜100に
導入される約85℃の熱湯の量が排気段階の95℃の熱
湯による予熱と排気に必要な量と略同じになったら、8
5℃の熱湯の導入を停止する。After completion of the sterilization step, a heat recovery step is performed. First, hot water of about 85 ° C. stored in the second tank 20 is sent to the sterilization pot 100 by the action of the pump 21 and sprayed from the top of the pot. This allows the cans at the sterilization temperature to be evenly and gradually cooled while condensing the steam in the kettle, minimizing the pressure difference between the inside and outside of the cans, eliminating the need to maintain compressed kettle pressure by adding compressed air, eliminating air. Electric energy used for compression can also be saved. 8
When exchanging heat with 5 ° C hot water to recover heat energy,
When the boiling water heated to 95 ° C has accumulated a considerable volume in the pot,
The water is started to be discharged from the bottom of the kettle and introduced into the first tank 10, so that the time required for the hot water to move out of the kettle can be saved. When the amount of the hot water of about 85 ° C. introduced into the sterilization pot 100 is substantially the same as the amount required for the preheating by the hot water of 95 ° C. and the evacuation in the evacuation stage, 8
Stop the introduction of 5 ° C hot water.
【0014】該熱回収段階の95℃の熱湯を放流完了
後、該放流する排水弁を閉め、普通の冷却水を殺菌釜1
00に導入し、釜頂からも吹き撒き、釜内の缶詰を均等
に冷却し、釜内上下部分の缶詰に略同じの冷却温度にす
る、これが冷却段階である。先に熱回収段階の熱交換を
経ているので、釜内の缶詰温度は既に低く、この冷却水
の温度も低くてよく、釜から出される缶詰の温度も低く
均等である。After the discharge of the hot water of 95 ° C. in the heat recovery stage is completed, the drain valve for discharging the water is closed, and ordinary cooling water is supplied to the sterilizing pot 1.
00, and also sprayed from the top of the kettle to uniformly cool the cans in the kettle so that the cooling temperature is approximately the same as that of the upper and lower cans in the kettle. This is the cooling stage. Since the heat exchange in the heat recovery stage has been performed first, the canning temperature in the kettle is already low, the temperature of the cooling water may be low, and the temperature of the canned discharged from the kettle is low and uniform.
【0015】又、排気段階を行う前、一部分の95℃の
熱湯を釜頂から吹き撒き、缶詰を洗うことができ、清浄
後の水は釜底から排出廃棄し、別に一部分の新しい水を
第二タンクに補充することにより、熱湯が缶詰に汚染さ
れたり、繰り返し循環使用による水質悪化等のの問題を
避けられる。Before the exhausting step, a part of the hot water of 95 ° C. can be sprayed from the top of the pot to wash the cans. The purified water is discharged from the bottom of the pot and discarded. By replenishing the two tanks, it is possible to avoid problems such as contamination of canned hot water and deterioration of water quality due to repeated use.
【0016】次に比較例と実施例を挙げて本発明を説明
するが、実施例は単に説明するだけで、本発明の範囲を
制限するものではない。Next, the present invention will be described with reference to comparative examples and examples, but the examples are merely illustrative and do not limit the scope of the present invention.
【0017】比較例:蒸気排気方式の殺菌方法を使用 殺菌すべき缶詰食品は350gの茶類飲料缶詰であり、
1缶最大の容量は330gである。殺菌釜は4×14f
t(D×L)横置式殺菌釜である。内には四つの籠があ
り、1籠には13缶×15缶×7層の製品があり、合計
1釜に5460缶ある。Comparative Example: Use of steam exhaust system sterilization method The canned food to be sterilized is 350 g of canned tea beverage.
The maximum capacity of one can is 330 g. Sterilization pot is 4 × 14f
It is a t (D × L) horizontal sterilization pot. There are four baskets inside, and one basket has 13 cans x 15 cans x 7 layers of products, with a total of 5460 cans per kettle.
【0018】予め缶詰食品を入れている釜内に飽和蒸気
を導入し排気を行う、釜内の空気は釜頂の排気弁と漏ら
し弁より排出させ、排気は圧力を0.32 kg/cm2 ゲージ
圧、時間7分に設定し、排気完了後、排気弁を閉め、続
けて蒸気を導入し、約2分で、釜内の蒸気圧力は0.32か
ら 0.92 kg/ cm2 ゲージ圧に上昇し、温度も目標の殺菌
温度118.5 ℃(相対飽和蒸気圧力 0.92 kg/ cm2 ゲージ
圧)に達し、該温度を20分維持して殺菌が完成してか
ら、蒸気の導入を中止し、排気弁を開き、蒸気を放出
し、冷却水を導入する。実験の結果は表1の通りであ
る。Saturated steam is introduced into the kettle in which canned food is previously introduced, and exhaust is performed. The air in the kettle is exhausted from the exhaust valve and the leak valve at the top of the kettle, and the pressure is reduced to 0.32 kg / cm 2 gauge pressure. After the evacuation was completed, the exhaust valve was closed, and steam was continuously introduced. In about 2 minutes, the steam pressure in the kettle increased from 0.32 to 0.92 kg / cm 2 gauge pressure, and the temperature was increased. reached sterilizing temperature 118.5 ° C. of the target (relative saturation vapor pressure 0.92 kg / cm 2 gauge pressure), the temperature from the sterilization is completed by keeping 20 minutes, stop the introduction of steam, open the exhaust valve, steam And introduce cooling water. Table 1 shows the results of the experiment.
【0019】 表1 蒸気使用量、kg 試験 排気 昇温 殺菌 合計 1 130 36 51 217 2 − − − 216 3 − − − 217 4 − − − 216 5 − − − 213 6 − − − 218 平均値 216Table 1 Amount of steam used, kg Test Exhaust temperature rise Sterilization Total
【0020】実施例:熱湯排気方式による殺菌方法を使
用 比較例1の缶詰食品と殺菌釜を本実施例の殺菌方法に使
用した。第一タンクから95℃の熱湯をポンプで缶詰を
予め入れている殺菌釜の底部に導入し、該殺菌釜の洩れ
管に設置している第一号液面計で水があると偵知した
ら、釜は既に満水で、空気も釜頂の排気弁から排出して
いることを示す。Example: Use of sterilization method by hot water exhaustion method The canned food and sterilization pot of Comparative Example 1 were used for the sterilization method of this example. When hot water of 95 ° C. is introduced from the first tank to the bottom of the sterilization pot in which cans are previously placed by a pump, and when the first level gauge installed in the leak pipe of the sterilization pot detects that water is present, Indicates that the kettle is already full and air has been exhausted from the exhaust valve at the top of the kettle.
【0021】満水信号が蒸気制御器に伝わり、釜頂から
蒸気を導入し、釜内の圧力が0.2 kg/ cm2 に上昇した
時、釜底から排水を始め、蒸気制御器の圧力を0.2 kg/
cm2 に設定し、排出した水は第二タンクに導入し、水温
は約85℃である。When the full signal is transmitted to the steam controller, steam is introduced from the top of the kettle, and when the pressure in the kettle rises to 0.2 kg / cm 2 , drainage is started from the bottom of the kettle, and the pressure of the steam controller is reduced to 0.2 kg. /
Set to cm 2 , the drained water was introduced into the second tank and the water temperature was about 85 ° C.
【0022】該殺菌釜の排水管に設置している第二号液
面計が釜内は無水と示したら、釜底の排水弁を閉める。
釜内無水を信号が蒸気制御器に伝わると、蒸気を導入
し、圧力を上げ、釜内の温度を118.5 ℃の殺菌温度に上
げる。When the second liquid level gauge installed in the drain pipe of the sterilizing pot indicates that the inside of the pot is anhydrous, the drain valve at the bottom of the pot is closed.
When a signal is transmitted to the steam controller indicating that water in the pot is anhydrous, steam is introduced, the pressure is increased, and the temperature in the pot is raised to a sterilization temperature of 118.5 ° C.
【0023】該殺菌温度を20分維持し、蒸気を閉め、
第二タンク内の85℃の熱湯をポンプで殺菌釜に導入
し、釜頂から吹き撒き、水が約半釜に達した後、釜下の
排水弁を開き、釜内の約95℃の熱湯を第一タンクに導
入し蓄え、更に1分後、第二タンクから導入する85℃
の水を中止し、釜内の熱湯を全部排出した後、排水弁を
閉める。次に30℃の冷却水を殺菌釜に導入し冷却を行
い、約7分後に釜は満水し、30℃の冷却水導入を中止
し、釜内の水を放出し、放水完了後、釜門を開けて殺菌
完了の缶詰食品を取り出す。その結果は表2の通りであ
る。The sterilization temperature is maintained for 20 minutes, the steam is shut off,
The hot water of 85 ° C in the second tank is introduced into the sterilizing pot with a pump and sprayed from the top of the pot. After the water reaches about half the pot, the drain valve under the pot is opened and the hot water of about 95 ° C in the pot is opened. Into the first tank and store it, and after one minute, 85 ° C introduced from the second tank
After the water in the kettle has been stopped and the hot water in the pot has been drained, the drain valve is closed. Next, cooling water of 30 ° C. was introduced into the sterilizing pot to cool the pot. After about 7 minutes, the pot was filled with water, the introduction of the cooling water at 30 ° C. was stopped, and the water in the pot was discharged. Open and take out the sterilized canned food. Table 2 shows the results.
【0024】 表2 蒸気使用量、kg 試験 排気 昇温 殺菌 合計 7 75 41 30 146 8 66 41 30 142 9 68 46 26 140 平均値 143Table 2 Amount of steam used, kg Test Exhaust temperature rise Temperature Sterilization Total
【0025】表1と2のデータを比較することにより、
本発明の熱湯排気方式の殺菌法は、伝統的の蒸気排気方
式の殺菌法より蒸気を節約できることが算出できる: By comparing the data in Tables 1 and 2,
It can be calculated that the hot water exhaust sterilization method of the present invention can save steam over the traditional steam exhaust sterilization method:
【0026】以上より、業者は本発明の方法は1回の殺
菌循環で34%の蒸気使用量を節約でき、2台のポンプ
の電気消耗量は7.5 HP×2 ×2.5 分で、メーターは約0.
5 度であり、費用は極僅かである。従って、長時間多数
回循環操作で節約する蒸気の使用量は非常に多く、甚だ
産業上の利用価値がある。From the above, it can be seen that the method of the present invention can save 34% of steam consumption in one sterilization cycle, the electric consumption of two pumps is 7.5 HP × 2 × 2.5 minutes, and the meter is about 0.
5 degrees and the cost is minimal. Therefore, the amount of steam saved by the circulation operation for a long time and a large number of times is very large, and has a great industrial value.
図1は本発明の殺菌方法の好ましい具体的実施方式のフ
ローチャートを示す。FIG. 1 shows a flowchart of a preferred specific embodiment of the sterilization method of the present invention.
Claims (1)
において、(a)殺菌すべき缶詰を予め入れている殺菌
釜に第一タンクから93−97℃の熱湯を導入し、殺菌
釜が満水するまで導入れた熱湯により釜内の空気を釜頂
から排出させ、該93−97℃の熱湯は缶詰と釜体を予
熱することにより83−87℃に低下することと、
(b)該釜内の83−87℃の熱湯が釜内に無くなるま
で殺菌釜の釜底から第二タンクに流出させ、該流出の開
始と共に該殺菌釜の頂部から蒸気を導入し、導入した蒸
気量は釜内正圧を保持するに充分であり、空気は釜内に
入らないことと、(c)該殺菌釜内の温度が予定の殺菌
温度に達するまで蒸気導入を続け、該温度を予定の殺菌
時間維持した後、蒸気導入を中止することと、(d)該
第二タンクの83−87℃の熱湯を殺菌釜に導入すると
共に、釜頂から吹き撒き、該導入された83−87℃の
熱湯は釜内の蒸気を冷却し、高温釜体及び釜内缶詰と熱
交換を行い、93−97℃に加熱され、一段の時間を経
た後、該殺菌釜内で93−97℃に加熱された熱湯を釜
底から流出し始め、第一タンクに導入させ、該83−8
7℃の熱湯が殺菌釜に導入される量を(a)の93−9
7℃の熱湯を該殺菌釜に導入する量と略同じにすること
と、(e)上記(d)にて93−97℃に加熱された熱
湯の流出し完了後、該殺菌釜に冷却水を導入し始め、釜
内の缶詰に冷却を行ってから、冷却された殺菌缶詰食品
を釜内より取り出すことを特徴とする殺菌釜による缶詰
食品に殺菌を行う方法。1. A method for sterilizing canned foods using a sterilizing pot, wherein (a) hot water at 93-97 ° C. is introduced from a first tank into a sterilizing pot in which cans to be sterilized are previously placed; The hot water of 93-97 ° C is lowered to 83-87 ° C by preheating the can and the kettle, with the hot water introduced therein until the air in the kettle is discharged from the top of the kettle.
(B) The hot water at 83-87 ° C. in the kettle was drained from the bottom of the sterilization kettle to the second tank until the hot water disappeared in the kettle, and steam was introduced from the top of the sterilization pot at the start of the outflow. The amount of steam is sufficient to maintain the positive pressure in the kettle. Air must not enter the kettle, and (c) steam introduction is continued until the temperature in the sterilization pot reaches a predetermined sterilization temperature. After the scheduled sterilization time is maintained, the introduction of steam is stopped, and (d) hot water of 83-87 ° C. in the second tank is introduced into the sterilization pot, and is sprayed from the top of the pot, and the introduced 83- The hot water of 87 ° C. cools the steam in the kettle, performs heat exchange with the high-temperature kettle body and the can in the kettle, is heated to 93-97 ° C., and after a period of time, 93-97 ° C. in the sterilizing pot. The heated hot water starts flowing out of the bottom of the kettle and is introduced into the first tank.
The amount of hot water of 7 ° C. introduced into the sterilization pot was adjusted to 93-9 of (a).
The amount of hot water of 7 ° C. is set to be substantially the same as the amount to be introduced into the sterilizing pot. (E) After the hot water heated to 93-97 ° C. in the above (d) is drained, cooling water is supplied to the sterilizing pot. A method of sterilizing canned food in a sterilizing pot, wherein the canned food in the pot is cooled after the introduction of the canned food, and then the cooled sterilized canned food is taken out from the pot.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5259276A JP2598874B2 (en) | 1993-09-22 | 1993-09-22 | Improved method of sterilizing canned foods with a sterilizing pot |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5259276A JP2598874B2 (en) | 1993-09-22 | 1993-09-22 | Improved method of sterilizing canned foods with a sterilizing pot |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07155150A JPH07155150A (en) | 1995-06-20 |
JP2598874B2 true JP2598874B2 (en) | 1997-04-09 |
Family
ID=17331848
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5259276A Expired - Lifetime JP2598874B2 (en) | 1993-09-22 | 1993-09-22 | Improved method of sterilizing canned foods with a sterilizing pot |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2598874B2 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4590140B2 (en) * | 2001-09-14 | 2010-12-01 | オリンパス株式会社 | High-pressure steam sterilizer and high-pressure steam sterilization method |
JP5192920B2 (en) * | 2008-06-19 | 2013-05-08 | サントリーホールディングス株式会社 | Heating and pressing system |
JP5093383B1 (en) * | 2011-06-03 | 2012-12-12 | 東洋製罐株式会社 | Retort sterilization method for packaged products |
CN109502532B (en) * | 2018-09-25 | 2019-11-26 | 江苏新美星包装机械股份有限公司 | A kind of process for sterilizing for sterile filling production line |
CN113115890B (en) * | 2019-12-31 | 2023-12-12 | 山东智汇环境工程有限公司 | Continuous sterilization system |
-
1993
- 1993-09-22 JP JP5259276A patent/JP2598874B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH07155150A (en) | 1995-06-20 |
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