JP2694149B2 - Food sterilization method - Google Patents

Food sterilization method

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Publication number
JP2694149B2
JP2694149B2 JP20653687A JP20653687A JP2694149B2 JP 2694149 B2 JP2694149 B2 JP 2694149B2 JP 20653687 A JP20653687 A JP 20653687A JP 20653687 A JP20653687 A JP 20653687A JP 2694149 B2 JP2694149 B2 JP 2694149B2
Authority
JP
Japan
Prior art keywords
ozone
water
treated water
food
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
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JP20653687A
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Japanese (ja)
Other versions
JPS6451071A (en
Inventor
武 椎野
寛 馬場
千秋 細井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Kakoki Kaisha Ltd
Original Assignee
Mitsubishi Kakoki Kaisha Ltd
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Priority to JP20653687A priority Critical patent/JP2694149B2/en
Publication of JPS6451071A publication Critical patent/JPS6451071A/en
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Publication of JP2694149B2 publication Critical patent/JP2694149B2/en
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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、食肉類、魚介類、または農産物などの食品
の殺菌方法に関する。 〔従来の技術〕 一般に、例えば食肉類の殺菌には、次亜塩素酸ソーダ
などの塩素系薬剤が幅広く使用されている。 なお、この塩素系薬剤の使用量の上限値は、現行の食
品衛生法上何ら規制されていないため、殺菌効果を高め
るために大量使用されているのが現状である。 〔発明が解決しようとする問題点〕 ところで、この塩素系薬剤を用いた殺菌方法では、使
用される塩素系薬剤の腐食性により機械設備の損耗を早
め、食品類の有機酸と反応して発癌物質であるトリハロ
メタンを生成させ、このトリハロメタンが食品内に残留
する恐れがある。 また、殺菌能力と薬剤の濃度のよる人体への害は比例
するので、前述したように殺菌効果を高めるためにこの
塩素系薬剤を大量使用することは、食品衛生という見地
に立つと好ましくない。 さらに、このように殺菌剤に塩素系薬剤を使用するた
め、殺菌された食品類への有機物の残留および殺菌処理
場内に塩素系薬剤独特の悪臭が発生するという問題があ
る。 さらにまた、近年、消費者団体などの強い要請を反映
して、残留塩素量の規制化の動きがあり、新しい殺菌方
法の採用が期待されている。 本発明はこのような従来技術の問題点および要望を背
景になされたもので、発癌性がなく、また品質を低下さ
せず、さらに殺菌された食品への残留および殺菌処理場
内の悪臭を解消できる食品の殺菌方法を提供するもので
ある。 〔問題点を解決するための手段〕 すなわち、本発明は、水に有機酸を添加するとともに
オゾンを溶解してオゾン含有処理水を調製し、そののち
該オゾン含有処理水を用いて食品を殺菌することを特徴
とする食品の殺菌方法を提供するものである。 ここで、本発明における有機酸とは、食品を効果的に
殺菌するためにオゾン含有処理水のpHを酸性に調節する
ためのもので、その添加方法は、水に有機酸自体を直接
添加してもよいし、またはこの有機酸を適宜濃度の水溶
液にして添加してもよい。 この有機酸としては、例えばクエン酸、酢酸、リンゴ
酸、酒石酸、乳酸などの食品衛生法上食品添加物として
許可されている有機酸を挙げることができる。 さらに、本発明でいう前記オゾン含有処理水は、食品
を殺菌するこれらの有機酸およびオゾンが含有された殺
菌用処理水である。 このオゾン含有処理水のpHは、3〜5、好ましくはpH
3〜4であり、pHが3未満であると腐蝕性により設備の
損耗を早め、また有機酸特有の臭いが食品に付き、食品
価値を損なう恐れがあり、一方pHが5を超えるとオゾン
との相乗効果が乏しいものとなり、殺菌効果が充分に発
揮できない。 また、このオゾン含有処理水のオゾン濃度は、1〜10
mg/l、好ましくは2〜5mg/lであり、1mg/l未満ではオゾ
ン濃度が低すぎて殺菌効果が充分でなく、一方10mg/lを
超えるとオゾン濃度が高すぎて経済的でないばかりか、
オゾンが大気中に放散して雰囲気を悪化し、またオゾン
の酸化作用により、食品によっては変質する可能性があ
る。 なお、食品の殺菌時におけるこのオゾン含有処理水の
温度は、通常、0〜30℃、好ましくは3〜10℃であり、
0℃未満であると温度が低すぎるために殺菌のための処
理時間が長くなりすぎる傾向にあり、一方30℃を超える
と温度が高くなりすぎオゾンの分散速度が速くなってか
えって殺菌効果が不充分となる。 また、このオゾン含有処理水による食品の殺菌処理時
間は、このオゾン含有処理水を食品にスプレーして殺菌
するスプレー方式の場合と、このオゾン含有処理水を満
たした処理水槽中で食品を処理して殺菌する方式の場合
とで異なるが、通常、数秒〜数十分である。 本発明のオゾン含有処理水の調製は、水に有機酸を添
加し、かつオゾンを溶解することにより行われるが、好
ましくは水に有機酸を添加させると同時にまたは添加さ
せたのちにオゾンを溶解させる方がよい。これは、あら
かじめ有機酸を溶解させた低pH域にオゾンを溶解させた
方がオゾンの分解速度が遅くなるためである。 以下、本発明の食品の殺菌方法を図面を用い、さらに
詳細に説明する。 なお、本発明の食品の殺菌方法を使用した食品の殺菌
装置として、食鳥屠体の殺菌装置を例にとる。 この殺菌装置は、第1図に示すように受水槽10、供給
ポンプ20、スプレー部30、pH調整系40、オゾン含有系5
0、コンベア60、および処理水槽70を備えている。 前記受水槽10は、水道供給される水Wを貯水しpH調整
するための槽であり、また供給ポンプ20は、オゾン含有
処理水W2を前記スプレー部30を介して食鳥屠体Sにスプ
レーさせるためのポンプである。 さらに、前記スプレー部30は、オゾン含有処理水W2を
食鳥屠体Sにスプレーするものである。 前記pH調整系40は、受水槽10内に供給された水WのpH
を食鳥屠体Sの殺菌を行うために調整するための系で、
酢酸溶液槽41および酢酸供給ポンプ42を有している。 この酢酸溶液槽41は、内部に酢酸溶液(有機酸)411
を貯液する槽で、また酢酸供給ポンプ42は、この酢酸溶
液槽41内の酢酸溶液411を前記受水槽10内に供給するた
めのポンプである。 前記オゾン含有系50は、前記pH調整系40とともに食鳥
屠体Sの殺菌を行うために、受水槽10内の水W1中にオゾ
ンO3を溶解させてオゾン含有処理水W2を調製するための
系で、酸素ボンベ51、オゾナイザ52、オゾン溶解ループ
部53、気液分離槽54、および排オゾン処理カラム55を有
している。 このオゾナイザ52は、酸素ボンベ51から送られた酸素
ガスから放電や紫外線放射などを利用してオゾンO3を発
生させるための装置で、前記受水槽10内に供給される水
道の水Wの一部が冷却水として用いられている。 また、オゾン溶解ループ部53は、水W1にオゾンを溶解
させるための環状装置で、実際に水W1にオゾンO3を溶解
させるエジェクタ531と、このオゾン溶解ループ部53に
受水槽10内の水W1を供給するとともに、この水W1中のオ
ゾンO3の含有率を高めるためにオゾンO3の循環溶解を行
わせるための循環ポンプ532を有している。 なお、このオゾン溶解ループ部53において、水Wは、
オゾンと酢酸溶液411とを含むオゾン含有処理水W2とな
る。 さらに、気液分離槽54は、このオゾン溶解ループ部53
内のオゾン含有処理水W2を気液分離する槽で、この気液
分離槽54の底部は所定オゾン濃度のオゾン含有処理水W2
を前記供給ポンプ20を介してスプレー部30に供給するた
めに前記供給ポンプ20と連通され、またこの上部は気体
を分離したオゾン含有処理水W2の一部を受水槽10に戻す
ために受水槽10と連通される。 さらに、この塔上部は、分離された気体中の未溶解オ
ゾンを処理して大気放出させるために排オゾン処理カラ
ム55に連通されている。 この本発明の食品の殺菌方法を採用した殺菌装置の作
用は、同じく第1図に示すようにまずあらかじめ送水さ
れた水Wが受水槽10内に貯水されるとともに、この受水
槽10内にpH調整系40から所定量の酢酸溶液411が供給さ
れ、pHが調整された水W1が生成される。 一方、オゾン含有系50では、酸素ボンベ51内の酸素ガ
スがオゾナイザ52内に供給され放電や紫外線照射などに
よりオゾンO3が生成される。 そののち、前記受水槽10内のpHが低下した水W1は、循
環ポンプ532により循環され、一方生成したオゾンO3
含有する気体はエジェクタ531に送られ、ここでpHを調
整された水W1に混合してオゾンO2が溶解しオゾン含有処
理水W2となる。 次にまた、このオゾン含有処理水W2は、気液分離槽54
へ送られ、未溶解オゾンを含有した気体を分離し所定オ
ゾン濃度のオゾン含有処理水W2が得られる。オゾン含有
処理水W2は、供給ポンプ20でスプレー部30へ送られ、コ
ンベア60、あるいは処理水槽70に取り付けられた食鳥屠
体Sにスプレーまたは浸漬して殺菌する。 なお、気体を分離したオゾン含有処理水W2の一部は受
水槽10に戻され、また分離された未溶解オゾンO3含有気
体は排オゾン処理カラム55を介して大気に放出される。 このようにすることによって、発癌性がなく、また品
質を低下させずに、食品を殺菌することが可能であり、
さらに殺菌された食品への有害物残留および殺菌処理場
内の悪臭を解消することができる。 なお、本発明の食品の殺菌方法が適用される殺菌装置
は、これに限定されるものでない。 〔実施例〕 以下、実施例を挙げ、本発明をさらに具体的に説明す
るが、本発明は以下の実施例に限定されるものではな
い。 実施例1 5℃に保冷した水に氷酢酸を添加しpHを4.0に調整し
たのち、オゾン含有気体を吹き込んでオゾン濃度を3mg/
lに調整したオゾン含有処理水を調整して、三角フラス
コに100ml採取した。このオゾン含有処理水中に、107
/mlのサルモネラ菌を1mlを添加し、第1表の処理条件で
殺菌処理した。結果を第1表に示す。 実施例2 オゾン含有処理水のオゾン濃度を5mg/lに調整した以
外は、実施例1と同様に実験した。 結果を第1表に示す。 実施例3 水のpHを3.0に調整した以外は、実施例1と同様に実
験した。結果を第1表に示す。 実施例4 水の温度を24℃に保冷した以外は、実施例1と同様に
実験した。結果を第1表に示す。 比較例1 5℃に保冷した水100mlを三角フラスコに採取し、氷
酢酸を添加してpHを4.0に調整した処理水を調製した。
この処理水中に107個/mlのサルモネラ菌を1ml添加し、
第1表の処理条件で殺菌処理した。結果を第1表に示
す。 比較例2 水のpHを3.0に調整した以外は、比較例1と同様に実
験した。結果を第1表に示す。 比較例3 5℃に保冷した水100mlを三角フラスコに採取し、オ
ゾン含有気体を吹き込んでオゾン濃度を3mg/lに調整し
た処理水を調製した。 その処理水中に107個/mlのサルモネラ菌を1mlを添加
し、第1表の処理条件で殺菌処理した。結果を第1表に
示す。 比較例4 処理水のオゾン濃度を5mg/lに調整した以外は、比較
例1と同様に実験した。結果を第1表に示す。 第1表から明らかなように、酢酸水溶液単独またはオ
ゾン水単独に比べ、両者を併用した本発明のオゾン含有
処理水の方が、顕著な殺菌効果が得られることが分か
る。 〔発明の効果〕 本発明は、このように水に有機酸を添加するとともに
オゾンを溶解させてオゾン含有処理水を調製し、そのの
ち該オゾン含有処理水を用いて食品を殺菌するため、発
癌性がなく、また品質を低下させず、さらに殺菌された
食品への有害物残留および殺菌処理場内の悪臭を解消で
きるという効果が得られる。
TECHNICAL FIELD The present invention relates to a method for sterilizing foods such as meats, seafood, and agricultural products. [Prior Art] Generally, for sterilization of meat, for example, chlorine-based agents such as sodium hypochlorite are widely used. The upper limit of the amount of the chlorine-based drug used is not regulated under the current Food Sanitation Law, and is currently used in large amounts to enhance the bactericidal effect. [Problems to be solved by the invention] By the way, in the sterilization method using this chlorine-based chemical, the corrosiveness of the chlorine-based chemical used accelerates the wear of mechanical equipment and causes carcinogenesis by reacting with organic acids of foods. The substance, trihalomethane, is produced, and this trihalomethane may remain in food. Further, since the sterilizing ability and the harmful effect on the human body depending on the concentration of the drug are proportional to each other, it is not preferable from the viewpoint of food hygiene to use a large amount of this chlorine-based drug to enhance the bactericidal effect as described above. Further, since the chlorine-based drug is used as the bactericide in this way, there is a problem that an organic substance remains on the sterilized food and a malodor peculiar to the chlorine-based drug is generated in the sterilization treatment site. Furthermore, in recent years, reflecting the strong demand of consumer organizations and the like, there is a movement to regulate the amount of residual chlorine, and adoption of a new sterilization method is expected. The present invention has been made in view of such problems and demands of the conventional technology, has no carcinogenicity, does not deteriorate quality, and can eliminate residual sterilized food and odor in a sterilization plant. A method for sterilizing food is provided. [Means for Solving Problems] That is, the present invention is to prepare an ozone-containing treated water by adding an organic acid to water and dissolving ozone, and then sterilize food using the ozone-containing treated water. The present invention provides a method for sterilizing foods, which comprises: Here, the organic acid in the present invention is for adjusting the pH of the ozone-containing treated water to be acidic in order to effectively sterilize the food, and the addition method is to add the organic acid itself to water directly. Alternatively, this organic acid may be added in the form of an aqueous solution having an appropriate concentration. Examples of the organic acid include citric acid, acetic acid, malic acid, tartaric acid, lactic acid, and other organic acids permitted as food additives under the Food Sanitation Act. Further, the treated water containing ozone referred to in the present invention is treated water for sterilization, which contains these organic acids for sterilizing food and ozone. The pH of the ozone-containing treated water is 3 to 5, preferably pH.
If it is 3 to 4 and the pH is less than 3, corrosion of the equipment is accelerated due to corrosiveness, and the odor peculiar to the organic acid may be attached to the food, which may impair the food value. The synergistic effect of is poor and the bactericidal effect cannot be fully exerted. The ozone concentration of the treated water containing ozone is 1 to 10
mg / l, preferably 2-5 mg / l. If it is less than 1 mg / l, the ozone concentration is too low and the bactericidal effect is not sufficient, while if it exceeds 10 mg / l, the ozone concentration is too high and it is not economical. ,
Ozone diffuses into the atmosphere and deteriorates the atmosphere, and the oxidizing action of ozone may change the quality of some foods. The temperature of the ozone-containing treated water during sterilization of food is usually 0 to 30 ° C, preferably 3 to 10 ° C.
If it is lower than 0 ° C, the temperature is too low and the treatment time for sterilization tends to be too long, while if it is higher than 30 ° C, the temperature becomes too high and the ozone dispersion speed becomes too fast, and the bactericidal effect becomes worse. Will be enough. In addition, the sterilization processing time of the food with this ozone-containing treated water is the case of the spray method in which this ozone-containing treated water is sprayed on the food and sterilized, and the food is treated in the treated water tank filled with this ozone-containing treated water. Although it differs from the case of the method of sterilizing by sterilization, it is usually several seconds to tens of minutes. The ozone-containing treated water of the present invention is prepared by adding an organic acid to water and dissolving the ozone, but preferably the ozone is dissolved at the same time as or after the addition of the organic acid to the water. It is better to let it. This is because the ozone decomposition rate becomes slower when ozone is dissolved in the low pH range where the organic acid is dissolved in advance. Hereinafter, the method for sterilizing food according to the present invention will be described in more detail with reference to the drawings. As a food sterilizer using the food sterilization method of the present invention, a sterilizer for a poultry carcass will be taken as an example. As shown in FIG. 1, this sterilizer includes a water receiving tank 10, a supply pump 20, a spray unit 30, a pH adjusting system 40, and an ozone containing system 5
0, a conveyor 60, and a treated water tank 70 are provided. The water receiving tank 10 is a tank for storing the water W to be supplied from the tap water and adjusting the pH, and the supply pump 20 sprays the ozone-containing treated water W2 onto the poultry carcass S through the spray unit 30. It is a pump for making. Further, the spray unit 30 sprays the ozone-containing treated water W2 onto the poultry carcass S. The pH adjusting system 40 controls the pH of the water W supplied into the water receiving tank 10.
Is a system for adjusting the sterilization of the carcass S of poultry,
It has an acetic acid solution tank 41 and an acetic acid supply pump 42. This acetic acid solution tank 41 has an acetic acid solution (organic acid) 411 inside.
The acetic acid supply pump 42 is a pump for supplying the acetic acid solution 411 in the acetic acid solution tank 41 into the water receiving tank 10. In order to sterilize the poultry carcass S together with the pH adjusting system 40, the ozone-containing system 50 dissolves ozone O 3 in the water W1 in the water receiving tank 10 to prepare the ozone-containing treated water W2. This system has an oxygen cylinder 51, an ozonizer 52, an ozone dissolution loop section 53, a gas-liquid separation tank 54, and an exhaust ozone treatment column 55. The ozonizer 52 is a device for generating ozone O 3 from the oxygen gas sent from the oxygen cylinder 51 by using discharge or ultraviolet radiation, and is one of the tap water W supplied to the water receiving tank 10. Part is used as cooling water. Also, ozone dissolution loop portion 53, an annular apparatus for dissolving ozone in water W1, the ejector 531 to actually dissolve ozone O 3 in water W1, the water receiving tank 10 to the ozone dissolution loop portion 53 A circulation pump 532 is provided to supply W1 and to circulate and dissolve ozone O 3 in order to increase the content of ozone O 3 in the water W1. In the ozone dissolution loop section 53, the water W is
It becomes ozone-containing treated water W2 containing ozone and acetic acid solution 411. Further, the gas-liquid separation tank 54 has the ozone dissolution loop portion 53.
Is a tank for separating the ozone-containing treated water W2 in the gas-liquid separation.
Is connected to the supply pump 20 in order to supply it to the spray section 30 via the supply pump 20, and the upper part thereof is a water receiving tank for returning a part of the ozone-containing treated water W2 from which gas has been separated to the water receiving tank 10. Communicated with 10. Further, the upper part of the tower is connected to an exhaust ozone treatment column 55 for treating the undissolved ozone in the separated gas and releasing it to the atmosphere. The action of the sterilizing apparatus adopting the food sterilizing method of the present invention is as follows. Similarly, as shown in FIG. 1, first, the water W previously sent is stored in the water receiving tank 10 and the pH in the water receiving tank 10 is increased. A predetermined amount of acetic acid solution 411 is supplied from the adjusting system 40, and pH-adjusted water W1 is produced. On the other hand, in the ozone-containing system 50, the oxygen gas in the oxygen cylinder 51 is supplied into the ozonizer 52, and ozone O 3 is generated by discharge or ultraviolet irradiation. After that, water W1 which pH in the receiving tank 10 is lowered is circulated by a circulation pump 532, whereas the gas containing ozone O 3 generated is sent to the ejector 531, wherein the adjusted the pH of water W1 Ozone O 2 is dissolved by mixing with and becomes ozone-containing treated water W 2. Next, the ozone-containing treated water W2 is again used in the gas-liquid separation tank 54.
Is sent to and the gas containing undissolved ozone is separated to obtain ozone-containing treated water W2 having a predetermined ozone concentration. The ozone-containing treated water W2 is sent to the spray unit 30 by the supply pump 20, and is sprayed or dipped in the poultry carcass S attached to the conveyor 60 or the treated water tank 70 for sterilization. A part of the ozone-containing treated water W2 from which the gas has been separated is returned to the water receiving tank 10, and the separated undissolved ozone O 3 -containing gas is released to the atmosphere via the exhaust ozone processing column 55. By doing this, it is possible to sterilize the food without carcinogenicity and without degrading the quality,
Further, it is possible to eliminate the harmful substances remaining in the sterilized food and the bad odor in the sterilization plant. The sterilizing apparatus to which the food sterilizing method of the present invention is applied is not limited to this. [Examples] Hereinafter, the present invention will be described more specifically with reference to Examples, but the present invention is not limited to the following Examples. Example 1 Glacial acetic acid was added to water kept at 5 ° C. to adjust the pH to 4.0, and then an ozone-containing gas was blown in to adjust the ozone concentration to 3 mg /
The treated water containing ozone adjusted to 1 was adjusted to 100 ml in an Erlenmeyer flask. In this ozone-containing treated water, 10 7
1 ml of Salmonella / ml was added and sterilized under the treatment conditions shown in Table 1. The results are shown in Table 1. Example 2 An experiment was performed in the same manner as in Example 1 except that the ozone concentration of the treated water containing ozone was adjusted to 5 mg / l. The results are shown in Table 1. Example 3 An experiment was performed in the same manner as in Example 1 except that the pH of water was adjusted to 3.0. The results are shown in Table 1. Example 4 An experiment was performed in the same manner as in Example 1 except that the temperature of water was kept at 24 ° C. The results are shown in Table 1. Comparative Example 1 100 ml of water cooled at 5 ° C. was collected in an Erlenmeyer flask, and glacial acetic acid was added to prepare treated water having a pH of 4.0.
To this treated water, add 1 ml of 10 7 / ml Salmonella,
Sterilization was performed under the treatment conditions shown in Table 1. The results are shown in Table 1. Comparative Example 2 The same experiment as in Comparative Example 1 was carried out except that the pH of water was adjusted to 3.0. The results are shown in Table 1. Comparative Example 3 100 ml of water cooled at 5 ° C. was sampled in an Erlenmeyer flask, and ozone-containing gas was blown thereinto to prepare treated water having an ozone concentration of 3 mg / l. 1 ml of 10 7 cells / ml of Salmonella was added to the treated water and sterilized under the treatment conditions shown in Table 1. The results are shown in Table 1. Comparative Example 4 The same experiment as in Comparative Example 1 was performed except that the ozone concentration of the treated water was adjusted to 5 mg / l. The results are shown in Table 1. As is clear from Table 1, the ozone-containing treated water of the present invention in which both of them are used in combination has a more remarkable bactericidal effect than the acetic acid aqueous solution alone or the ozone water alone. [Effects of the Invention] The present invention thus prepares an ozone-containing treated water by adding an organic acid to water and dissolving ozone, and then sterilizes a food product using the ozone-containing treated water, thus causing carcinogenesis. In addition, it is possible to obtain the effects of eliminating harmful substances in the sterilized food and eliminating the bad odor in the sterilization plant, without any deterioration in quality and without degrading the quality.

【図面の簡単な説明】 第1図は本発明の食品の殺菌方法に使用される食品の殺
菌装置の1実施例を示す工程図である。 S;食鳥屠体(食品) W;水 10;受水槽 20;供給ポンプ 30;スプレー部 40;pH調整系 50;オゾン含有系 60;コンベア 70;処理水槽
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a process diagram showing one embodiment of a food sterilizing apparatus used in the food sterilizing method of the present invention. S; Poultry carcass (food) W; Water 10; Water tank 20; Supply pump 30; Spray unit 40; pH adjusting system 50; Ozone-containing system 60; Conveyor 70; Treated water tank

Claims (1)

(57)【特許請求の範囲】 1.水に有機酸を添加するとともにオゾンを溶解してオ
ゾン含有処理水を調製し、そののち該オゾン含有処理水
を用いて食品を殺菌することを特徴とする食品の殺菌方
法。 2.前記オゾン含有処理水の調製は、水に有機酸を添加
すると同時に、または添加したのちにオゾンを溶解して
なる特許請求の範囲第1項記載の食品の殺菌方法。 3.オゾン含有処理水のpHが3〜5である特許請求の範
囲第1項または第2項記載の食品の殺菌方法。 4.オゾン含有処理水のオゾン濃度が1〜10mg/lである
特許請求の範囲第1項、第2項または第3項記載の食品
の殺菌方法。
(57) [Claims] A method for sterilizing a food, which comprises adding an organic acid to water and dissolving ozone to prepare ozone-containing treated water, and then sterilizing the food using the ozone-containing treated water. 2. The method for sterilizing food according to claim 1, wherein the ozone-containing treated water is prepared by dissolving the ozone at the same time as or after adding the organic acid to the water. 3. The method for sterilizing food according to claim 1 or 2, wherein the ozone-containing treated water has a pH of 3 to 5. 4. The method for sterilizing food according to claim 1, 2, or 3, wherein the ozone-containing treated water has an ozone concentration of 1 to 10 mg / l.
JP20653687A 1987-08-21 1987-08-21 Food sterilization method Expired - Lifetime JP2694149B2 (en)

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JP20653687A JP2694149B2 (en) 1987-08-21 1987-08-21 Food sterilization method

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JP2694149B2 true JP2694149B2 (en) 1997-12-24

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Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03164155A (en) * 1989-11-22 1991-07-16 Aichi Pref Gov Sterilization of food or packaging material with alternate or mixed treatment using ozone and alcohol or organic acid
US5858443A (en) * 1996-05-13 1999-01-12 Ecolab, Inc. Process for effecting microbial control and reducing slime growth on hard surfaces in food processing equipment using inline ozonation
US20030070691A1 (en) * 2000-08-03 2003-04-17 Anthony Giletto Biocide formation via ozonation
US8486331B2 (en) * 2008-05-02 2013-07-16 Han Sup Uhm Sterilization effects of acidic ozone water

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