JP2736578B2 - Food salt water treatment equipment - Google Patents
Food salt water treatment equipmentInfo
- Publication number
- JP2736578B2 JP2736578B2 JP32784291A JP32784291A JP2736578B2 JP 2736578 B2 JP2736578 B2 JP 2736578B2 JP 32784291 A JP32784291 A JP 32784291A JP 32784291 A JP32784291 A JP 32784291A JP 2736578 B2 JP2736578 B2 JP 2736578B2
- Authority
- JP
- Japan
- Prior art keywords
- salt water
- tank
- concentration
- treatment
- processing
- 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
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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/90—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in food processing or handling, e.g. food conservation
Landscapes
- Storage Of Fruits Or Vegetables (AREA)
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は食物の塩水処理装置に関
する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a food salt water treatment apparatus.
【0002】[0002]
【従来の技術】食物の塩水処理装置は鮮魚、精肉、果
物、野菜等各種の食物に適した所定濃度の塩水からなる
処理液、例えば所定濃度の塩化ナトリウム水溶液からな
る処理液に、処理すべき上記した食物を所定温度で所定
時間浸漬処理して鮮度を長期間保持させようとするもの
である。また、このような塩水処理装置においては、各
種食物の塩水処理中に雑菌が処理液に混入しまたは処理
液が汚染されて雑菌が繁殖するおそれがあり、これに対
処するため実開昭55−139694号公報、実開昭5
9−6494号公報、実開昭63−178488号公報
等には、処理液の殺菌を行う手段を備えた塩水処理装置
が示されている。これらの塩水処理装置においては、処
理液を殺菌する手段として紫外線、オゾン等を使用して
いる。2. Description of the Related Art A food salt water treatment apparatus is to be processed into a treatment liquid comprising a predetermined concentration of salt water suitable for various foods such as fresh fish, meat, fruits, vegetables, etc., for example, a treatment liquid comprising a predetermined concentration of sodium chloride aqueous solution. The above-mentioned food is immersed at a predetermined temperature for a predetermined time to maintain the freshness for a long time. Further, in such a salt water treatment apparatus, there is a possibility that various bacteria may be mixed into the treatment liquid or the treatment liquid may be contaminated during the salt water treatment of various foods and bacteria may proliferate. 139694, Shokai 5
JP-A-9-6494, JP-A-63-178488, and the like show a salt water treatment apparatus provided with a means for sterilizing a treatment liquid. In these salt water treatment apparatuses, ultraviolet rays, ozone, and the like are used as means for sterilizing the treatment liquid.
【0003】[0003]
【発明が解決しようとする課題】ところで、オゾンが殺
菌力を有していることはよく知られていることである
が、オゾンの殺菌効果を十分に発揮させるにはオゾンを
処理液内へ高濃度に溶解させる必要があり、このため高
濃度のオゾンを含む気体を処理液中に供給して撹拌しつ
つ溶解させるものである。このため、処理液がその中の
蛋白質、脂肪等の汚染物質に起因して泡立ち、この泡が
処理した食物や処理槽、その他の構成部材に付着して汚
染する。また、オゾンの処理液内への供給量に対して処
理液内への溶解量が低いため、空気中に放出されるオゾ
ンの量が多く作業従事者の健康を損ねるおそれがある。
これらの問題を解消するために処理液内へのオゾンの供
給量を減少させると、オゾンによる殺菌効果が大きく低
下するという問題が生じる。It is well known that ozone has a bactericidal activity. However, in order to sufficiently exert the bactericidal effect of ozone, it is necessary to introduce ozone into the processing solution. It is necessary to dissolve it in a concentration, and for this reason, a gas containing a high concentration of ozone is supplied into the processing liquid and dissolved while stirring. Therefore, the processing liquid foams due to contaminants such as proteins and fats therein, and the foam adheres to and contaminates the processed food, the processing tank, and other components. Further, since the amount of ozone dissolved in the processing solution is lower than the amount of ozone supplied into the processing solution, a large amount of ozone is released into the air, which may impair the health of workers.
If the supply amount of ozone into the processing liquid is reduced in order to solve these problems, there arises a problem that the sterilization effect of ozone is greatly reduced.
【0004】また、紫外線を使用する手段においては、
紫外線はオゾンに比較して殺菌力がかなり低いことから
処理液の殺菌効果がさほど期待できず、また紫外線が透
過する部位のみが殺菌されるにすぎないため処理液全体
を殺菌することは難しく、処理液全体の殺菌を短時間に
行うことは不可能である。なお、塩素系の殺菌剤を使用
することも考えられるが、このような手段においては殺
菌剤の原液を希釈して使用する方法が採られるため濃度
管理が難しく、また使用する毎に殺菌剤が消費されるこ
とから処理液自体に殺菌効果を持続させることができな
い。従って、本発明の目的はこれらの問題に対処するこ
とにある。[0004] In the means using ultraviolet light,
Ultraviolet rays have a considerably lower sterilizing power compared to ozone, so the sterilizing effect of the processing liquid can not be expected so much, and it is difficult to sterilize the entire processing liquid because only the part through which ultraviolet rays pass is sterilized, It is impossible to sterilize the entire treatment liquid in a short time. It is also conceivable to use a chlorine-based disinfectant, but in such a method, it is difficult to control the concentration because a method of diluting the undiluted solution of the disinfectant is used. Since it is consumed, the sterilization effect cannot be maintained in the treatment liquid itself. Accordingly, it is an object of the present invention to address these problems.
【0005】[0005]
【課題を解決するための手段】本発明に係る食物の塩水
処理装置は、所定濃度の塩水からなる処理液を収容する
処理槽と、同処理槽へ供給する塩水を収容する塩水収容
槽と、同塩水収容槽の塩水を前記処理槽へ供給する供給
系路に配設され陽極および陰極間に供給された塩水を電
解して次亜塩素酸ナトリウムを生成する電解槽とを備え
たことを特徴とするものである。According to the present invention, there is provided a food salt water treatment apparatus, comprising: a treatment tank for accommodating a treatment liquid composed of salt water having a predetermined concentration; a salt water accommodation tank for accommodating salt water supplied to the treatment tank; An electrolytic tank disposed in a supply line for supplying the salt water of the salt water storage tank to the treatment tank and electrolyzing the salt water supplied between the anode and the cathode to generate sodium hypochlorite. It is assumed that.
【0006】また、本発明に係る食物の処理装置は、所
定濃度の塩水からなる処理液を収容する処理槽と、同処
理槽へ供給する塩水を収容する塩水収容槽と、同塩水収
容槽の塩水を前記処理槽へ供給する供給系路に配設され
陽極および陰極間に供給された塩水を電解して次亜塩素
酸を生成する電解槽とを備えたことを特徴とするもので
ある。[0006] Further, a food processing apparatus according to the present invention comprises a processing tank for storing a processing solution composed of salt water having a predetermined concentration, a salt water storage tank for storing salt water supplied to the processing tank, and a salt water storage tank. An electrolytic tank is provided in a supply system for supplying salt water to the treatment tank and electrolyzes the salt water supplied between the anode and the cathode to generate hypochlorous acid.
【0007】これらの塩水処理装置においては、前記塩
水収容槽内の塩水の塩濃度が前記処理槽内の所定濃度の
塩水からなる処理液の塩濃度と同一であることが好まし
く、また塩水としては塩化ナトリウム水溶液が好まし
い。さらにまた、前記処理槽が処理液を冷却する冷却手
段を備えていて、冷塩水処理が可能であることが好まし
い。In these salt water treatment apparatuses, it is preferable that the salt concentration of the salt water in the salt water storage tank is the same as the salt concentration of the treatment liquid composed of a predetermined concentration of salt water in the treatment tank. An aqueous sodium chloride solution is preferred. Furthermore, it is preferable that the treatment tank is provided with a cooling means for cooling the treatment liquid, and is capable of performing cold salt water treatment.
【0008】[0008]
【発明の作用・効果】このような構成の食物の塩水処理
装置においては、塩水収容槽から処理槽内へ塩水を供給
して同処理槽内に所定濃度の塩水からなる処理液を収容
することができるとともに、処理液が減少した場合には
その都度塩水収容槽から処理槽へ塩水を供給して補うこ
とができる。また、次亜塩素酸ナトリウムおよび次亜塩
素酸は殺菌作用があるとともに塩水に対して十分な量を
溶解させることができるため、塩水収容槽から処理槽へ
の塩水の供給時に電解槽を作動させて供給系路を流動す
る塩水を電解すれば、塩水中に次亜塩素酸ナトリウムま
たは次亜塩素酸が発生して塩水とともに処理槽内に供給
され、処理液に容易に溶解される。In the apparatus for treating salt water of food having such a constitution, the salt water is supplied from the salt water storage tank into the treatment tank, and the treatment liquid comprising a predetermined concentration of salt water is accommodated in the treatment tank. In addition, when the treatment liquid is reduced, the salt water can be supplied to the treatment tank from the salt water storage tank and supplemented each time. Also, since sodium hypochlorite and hypochlorous acid have a bactericidal action and can dissolve a sufficient amount in salt water, the electrolytic tank is operated when supplying salt water from the salt water storage tank to the treatment tank. When the salt water flowing through the supply system is electrolyzed, sodium hypochlorite or hypochlorous acid is generated in the salt water, supplied to the treatment tank together with the salt water, and easily dissolved in the treatment liquid.
【0009】このため、処理液中の次亜塩素酸ナトリウ
ムまたは次亜塩素酸の濃度が所定の濃度より低下した場
合等適宜の時点で電解槽を作動させて塩水を電解すれ
ば、処理液に次亜塩素酸ナトリウムまたは次亜塩素酸に
起因する殺菌作用を保持させることができ、処理液中の
雑菌を殺菌することができる。この場合、処理液を殺菌
するためにオゾン、紫外線、その他の殺菌剤等を使用す
ることがない。従って、本発明に係る塩水処理装置によ
れば、オゾンの使用に起因する食物および装置等への汚
染、作業従事者の健康への影響、殺菌効果等の問題を解
消することができ、また紫外線の使用に起因する殺菌効
果の問題、殺菌剤の使用に起因する殺菌効果および殺菌
剤の濃度管理等の問題を解消することができる。For this reason, when the concentration of sodium hypochlorite or hypochlorous acid in the treatment liquid falls below a predetermined concentration, for example, by operating the electrolytic cell to electrolyze the salt water, the treatment liquid can be treated. The bactericidal action caused by sodium hypochlorite or hypochlorous acid can be maintained, and germs in the treatment liquid can be sterilized. In this case, ozone, ultraviolet rays, other germicides, etc. are not used to sterilize the processing liquid. Therefore, according to the salt water treatment apparatus according to the present invention, it is possible to eliminate problems such as contamination of food and equipment due to the use of ozone, influence on health of workers, sterilization effect, and the like. The problem of the bactericidal effect resulting from the use of the bactericide, the germicidal effect resulting from the use of the bactericide, and the problem of controlling the concentration of the bactericide can be solved.
【0010】[0010]
【実施例】以下本発明の実施例を図面に基づいて説明す
るに、図1には本発明の第1実施例に係る塩水処理装置
が示されている。当該塩水処理装置10は処理槽11、
第1塩水供給手段12および電解槽13を備えるととも
に、処理水冷却手段14、第2塩水供給手段15および
制御手段16を備えている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 shows a salt water treatment apparatus according to a first embodiment of the present invention. The salt water treatment device 10 includes a treatment tank 11,
The apparatus includes a first salt water supply unit 12 and an electrolytic cell 13, and further includes a treated water cooling unit 14, a second salt water supply unit 15, and a control unit 16.
【0011】処理槽11は隔壁11aにより内部を処理
室11bと冷却室11cとに区画されており、連通管路
11dを介してこれら両室11b,11cが互いに連通
され、かつ連通管路11dには循環ポンプ11eが介装
されている。処理槽11の冷却室11cには冷却手段1
4を構成する冷却器14aが配設されている。冷却器1
4aはコンプレッサ14bを備え、循環系路14cを介
して冷却器14aに冷媒を循環させることにより、冷却
室11c内の処理液を冷却する。また、循環ポンプ11
eの駆動により冷却室11c内の処理液が処理室11b
内へ流入し、かつ処理室11b内の処理液が隔壁11a
上を乗り越えて冷却室11c内に流入し、処理液全体が
均一に冷却される。The inside of the processing tank 11 is divided into a processing chamber 11b and a cooling chamber 11c by a partition wall 11a. Is provided with a circulation pump 11e. The cooling means 11 is provided in the cooling chamber 11c of the processing tank 11.
4 is provided with a cooler 14a. Cooler 1
4a includes a compressor 14b, and cools the processing liquid in the cooling chamber 11c by circulating the refrigerant to the cooler 14a via the circulation path 14c. The circulation pump 11
e drives the processing liquid in the cooling chamber 11c to the processing chamber 11b.
And the processing solution in the processing chamber 11b flows into the partition 11a.
The liquid flows over the cooling chamber 11c, and is uniformly cooled.
【0012】第1塩水供給手段12は塩水収容槽12
a、塩水収容槽12aと電解槽13とを連通する連通管
路12bに配設された供給ポンプ12c、電磁開閉弁1
2d(第1開閉弁)を備えている。塩水収容槽12aに
は制御手段16を構成する第3濃度センサ16fとフロ
ートスイッチ12fとが配設されていて、その上方に給
水管路17aが臨んでいる。第3濃度センサ16fは塩
水収容槽12a内の塩化ナトリウム濃度を検出する機能
を備えている。第1塩水供給手段12においては、供給
ポンプ12cを駆動させかつ第1開閉弁12dを開くこ
とにより塩水収容槽12a内の塩化ナトリウム水溶液が
電解槽13に供給される。The first salt water supply means 12 includes a salt water storage tank 12
a, a supply pump 12c disposed in a communication pipe 12b that connects the salt water storage tank 12a and the electrolytic tank 13, and an electromagnetic on-off valve 1
2d (first on-off valve) is provided. A third concentration sensor 16f and a float switch 12f constituting the control means 16 are disposed in the salt water storage tank 12a, and a water supply pipe 17a faces above the third concentration sensor 16f. The third concentration sensor 16f has a function of detecting the concentration of sodium chloride in the salt water storage tank 12a. In the first salt water supply means 12, the supply pump 12c is driven and the first on-off valve 12d is opened, whereby the aqueous sodium chloride solution in the salt water storage tank 12a is supplied to the electrolytic tank 13.
【0013】電解槽13はケーシング内に陽極13aと
陰極13bとを備え、これら両極13a,13b間が塩
化ナトリウム水溶液の通路に形成されている。電解槽1
3においては、両電極13a,13b間に電圧が印加さ
れると、通路を流動する塩化ナトリウム水溶液を電気分
解して次亜塩素酸ナトリウムを生成する。生成された次
亜塩素酸ナトリウムは塩化ナトリウム水溶液とともにケ
ーシングから流出して処理槽11に供給される。The electrolytic cell 13 has an anode 13a and a cathode 13b in a casing, and a space for the aqueous solution of sodium chloride is formed between the electrodes 13a and 13b. Electrolyzer 1
In 3, when a voltage is applied between the electrodes 13a and 13b, the sodium chloride aqueous solution flowing through the passage is electrolyzed to generate sodium hypochlorite. The generated sodium hypochlorite flows out of the casing together with the aqueous sodium chloride solution and is supplied to the treatment tank 11.
【0014】第2塩水供給手段15は塩化ナトリウム水
溶液を収容する第2塩水収容槽15a、第1供給管路1
5bおよび第2供給管路15cにそれぞれ配設された電
磁開閉弁15d,15eを備えている。第2塩水収容槽
15内には第1塩水収容槽12a内の塩水よりも高い濃
度の塩化ナトリウム水溶液が収容されていて、第2開閉
弁15dが開かれると第2塩水収容槽15a内の塩水が
第1塩水収容槽12aに供給され、かつ第3開閉弁15
eが開かれると第2塩水収容槽15a内の塩水が処理槽
11に供給される。The second salt water supply means 15 includes a second salt water storage tank 15a for storing an aqueous solution of sodium chloride, a first supply line 1
5b and the second supply pipe 15c are provided with electromagnetic on-off valves 15d and 15e, respectively. The second salt water storage tank 15 stores a sodium chloride aqueous solution having a higher concentration than the salt water in the first salt water storage tank 12a, and when the second on-off valve 15d is opened, the salt water in the second salt water storage tank 15a is opened. Is supplied to the first salt water storage tank 12a and the third on-off valve 15
When e is opened, the salt water in the second salt water storage tank 15a is supplied to the processing tank 11.
【0015】制御手段16は第1,第2,第3ントロー
ラ16a,16b,16cを備えるとともに、次亜塩素
酸ナトリウムの濃度を検出する第1濃度センサ16d、
塩化ナトリウムの濃度を検出する第2および第3濃度セ
ンサ16e,16fを備えている。第1濃度センサ16
dは処理槽11内に配設されていて、処理槽11内の処
理液中の次亜塩素酸の濃度を検出して濃度検出信号を第
1コントローラ16aに出力する。第1コントローラ1
6aにおいては、処理液中の次亜塩素酸ナトリウム濃度
が所定の値より低い場合に濃度検出信号に基づいて供給
ポンプ12cを駆動させるとともに第1開閉弁12dを
開成し、かつ電解槽13の両電極13a,13b間に所
定の電圧を印加する。The control means 16 includes first, second and third controllers 16a, 16b and 16c, and a first concentration sensor 16d for detecting the concentration of sodium hypochlorite;
There are provided second and third concentration sensors 16e and 16f for detecting the concentration of sodium chloride. First density sensor 16
d is disposed in the processing tank 11 and detects the concentration of hypochlorous acid in the processing liquid in the processing tank 11 and outputs a concentration detection signal to the first controller 16a. First controller 1
In 6a, when the concentration of sodium hypochlorite in the treatment liquid is lower than a predetermined value, the supply pump 12c is driven based on the concentration detection signal, the first opening / closing valve 12d is opened, and A predetermined voltage is applied between the electrodes 13a and 13b.
【0016】これにより、第1塩水収容槽12a内の塩
水が電解槽13内に供給され、塩水は電解槽13内を流
動する間に電気分解を受けて次亜塩素酸ナトリウムが生
成される。生成された次亜塩素酸ナトリウムは塩水とと
もに処理槽11に供給され、処理液中の次亜塩素酸ナト
リウム濃度を所定の値に調整する。処理液中の次亜塩素
酸ナトリウム濃度が所定の値に調整されると、第1コン
トローラ16aは第1濃度センサ16dからの濃度検出
信号に基づき供給ポンプ12cの駆動を停止するととも
に第1開閉弁12dを閉成して、処理槽11への塩水お
よび次亜塩素酸ナトリウムの供給を停止する。As a result, the salt water in the first salt water storage tank 12a is supplied into the electrolytic tank 13, and the salt water undergoes electrolysis while flowing in the electrolytic tank 13 to generate sodium hypochlorite. The generated sodium hypochlorite is supplied to the treatment tank 11 together with the salt water, and the concentration of sodium hypochlorite in the treatment liquid is adjusted to a predetermined value. When the concentration of sodium hypochlorite in the processing liquid is adjusted to a predetermined value, the first controller 16a stops driving the supply pump 12c based on the concentration detection signal from the first concentration sensor 16d and sets the first on-off valve. 12d is closed, and the supply of the salt water and sodium hypochlorite to the treatment tank 11 is stopped.
【0017】第2濃度センサ16eは処理槽11内に配
設されていて、処理槽11内の処理液中の塩化ナトリウ
ム濃度を検出して濃度検出信号を第2コントローラ16
bに出力する。第2コントローラ16bにおいては、処
理液中の塩化ナトリウム濃度が所定の値より低い場合に
濃度検出信号に基づいて第3開閉弁15eを開成し、第
2塩水収容槽15aの高濃度の塩水を処理槽11へ供給
する。これにより、処理液中の塩化ナトリウム濃度が所
定の値に調整され、第2コントローラ16bは第2濃度
センサ16eからの検出信号に基づいて第3開閉弁15
eを閉成し、処理槽11への塩水の供給を停止する。The second concentration sensor 16e is disposed in the processing tank 11, detects the concentration of sodium chloride in the processing solution in the processing tank 11, and outputs a concentration detection signal to the second controller 16.
b. The second controller 16b opens the third on-off valve 15e based on the concentration detection signal when the concentration of sodium chloride in the treatment liquid is lower than a predetermined value, and treats the high concentration salt water in the second salt water storage tank 15a. Supply to tank 11. As a result, the concentration of sodium chloride in the processing solution is adjusted to a predetermined value, and the second controller 16b controls the third on-off valve 15 based on the detection signal from the second concentration sensor 16e.
e, and the supply of the salt water to the processing tank 11 is stopped.
【0018】第3濃度センサ16fは第1塩水収容槽1
2a内に配設されていて、第1塩水収容槽12a内の塩
水中の塩化ナトリウム濃度を検出して濃度検出信号を第
3コントローラ16cに出力する。第1塩水収容槽12
aにおいては、塩水の処理槽11への供給により塩水の
水位が低下するとフロートスイッチ12fが作動して、
給水管路17aに介装されている第4開閉弁17bを開
成して、第1塩水収容槽12aへ給水を行う。また、第
3コントローラ16cにおいては第1塩水収容槽12a
内の塩水中の塩化ナトリウム濃度が所定の値より低い場
合には、第3濃度センサ16fからの濃度検出信号に基
づいて第2開閉弁15dを開成し、第2塩水収容槽15
aの高濃度の塩水を第1塩水収容槽12aへ供給する。The third concentration sensor 16f is connected to the first salt water storage tank 1.
2a, which detects the concentration of sodium chloride in the salt water in the first salt water storage tank 12a and outputs a concentration detection signal to the third controller 16c. First salt water storage tank 12
In a, when the salt water level is lowered by the supply of the salt water to the treatment tank 11, the float switch 12f is operated,
The fourth on-off valve 17b interposed in the water supply pipe line 17a is opened to supply water to the first salt water storage tank 12a. In the third controller 16c, the first salt water storage tank 12a
When the concentration of sodium chloride in the salt water is lower than a predetermined value, the second on-off valve 15d is opened based on the concentration detection signal from the third concentration sensor 16f, and the second salt water storage tank 15 is opened.
The high-concentration salt water of a is supplied to the first salt water storage tank 12a.
【0019】このため、塩水中の塩化ナトリウム濃度が
所定の値に調整され、第3コントローラ16cは第3濃
度センサ16fからの濃度検出信号に基づいて第2開閉
弁15dを閉成し、第1塩水収容槽12aへの塩水の供
給を停止する。同時にフロートスイッチ12fが作動し
て第4開閉弁17bを閉成して給水を停止する。これに
より、第1塩水収容槽12aにおいては、塩水の塩化ナ
トリウム濃度および塩水の水位が常に所定の値に調整さ
れる。なお、第1塩水収容槽12a内の塩水の塩化ナト
リウム濃度は処理液中の塩化ナトリウム濃度とほぼ同一
の濃度に設定されている。Therefore, the concentration of sodium chloride in the salt water is adjusted to a predetermined value, and the third controller 16c closes the second on-off valve 15d based on the concentration detection signal from the third concentration sensor 16f, and the first controller 16c closes the first valve. The supply of the salt water to the salt water storage tank 12a is stopped. At the same time, the float switch 12f operates to close the fourth on-off valve 17b and stop water supply. Thus, in the first saltwater storage tank 12a, the sodium chloride concentration and the saltwater level of the saltwater are always adjusted to predetermined values. The concentration of sodium chloride in the salt water in the first salt water storage tank 12a is set to be substantially the same as the concentration of sodium chloride in the treatment liquid.
【0020】このように構成された食物の塩水処理装置
10においては、第1塩水供給手段12の第1塩水収容
槽12aから電解槽13を通して塩水が処理槽11へ供
給されて、所定濃度の塩化ナトリウムを含有する処理液
が処理槽11内に収容される。この間、電解槽13では
両電極13a,13b間に所定の電圧が印加されて次亜
塩素酸ナトリウムが生成されて塩水とともに処理槽11
に供給され、処理槽11内には所定の濃度の次亜塩素酸
ナトリウムおよび所定の濃度の塩化ナトリウムを含有す
る処理液が生成される。処理槽11内の処理液は冷却手
段14の駆動により所定の温度に冷却され、選定された
食物の塩水処理を行える状態とする。In the food salt water treatment apparatus 10 configured as described above, the salt water is supplied from the first salt water storage tank 12a of the first salt water supply means 12 to the treatment tank 11 through the electrolytic tank 13, and the salt water having a predetermined concentration is supplied. A processing solution containing sodium is contained in the processing tank 11. During this time, a predetermined voltage is applied between the electrodes 13a and 13b in the electrolytic cell 13 to generate sodium hypochlorite, and the treatment tank 11 is added together with the salt water.
And a processing solution containing a predetermined concentration of sodium hypochlorite and a predetermined concentration of sodium chloride is generated in the processing tank 11. The processing liquid in the processing tank 11 is cooled to a predetermined temperature by the driving of the cooling means 14 so that the selected food can be treated with salt water.
【0021】選定された食物はこのような処理槽11内
で所定時間浸漬されて塩水処理がなされ、必要により冷
水処理が施されて所定の保管場所に保管される。この塩
水処理の間に処理水に雑菌が発生した場合には、処理液
中の次亜塩素酸ナトリウムの殺菌作用により殺菌される
ため、処理液中に雑菌が繁殖することが防止される。ま
た、この殺菌のために処理液中の次亜塩素酸ナトリウム
の濃度が低下した場合には、第1濃度センサ16dから
の濃度検出信号に基づき第1コントローラ16aが供給
ポンプ12cを駆動するとともに第1開閉弁12dを開
成し、かつ電解槽13の両電極13a,13b間に所定
圧の電圧を印加する。The selected food is immersed in such a processing tank 11 for a predetermined time to be subjected to a salt water treatment, and if necessary, to a cold water treatment and stored in a predetermined storage place. If germs are generated in the treated water during the salt water treatment, the germs are sterilized by the bactericidal action of sodium hypochlorite in the treatment liquid, thereby preventing the germs from propagating in the treatment liquid. Further, when the concentration of sodium hypochlorite in the treatment liquid decreases due to this sterilization, the first controller 16a drives the supply pump 12c based on the concentration detection signal from the first concentration sensor 16d, One on-off valve 12d is opened, and a voltage of a predetermined pressure is applied between both electrodes 13a and 13b of the electrolytic cell 13.
【0022】このため、第1塩水収容槽12a内の塩水
が電解槽13へ供給されるとともに、供給された塩水が
電気分解されて塩水中に次亜塩素酸ナトリウムが生成さ
れ、生成された次亜塩素酸ナトリウムは塩水とともに処
理槽11に供給されて、処理液中の次亜塩素酸ナトリウ
ムの濃度を所定の濃度に調整して常に殺菌作用を保持す
る。この間、第1塩水供給手段12においてはフロート
スイッチ12f、第3濃度センサ16f、第3コントロ
ーラ16c等の作用により、第1塩水収容槽12a内の
塩水は所定の水位に保持されるとともに、塩化ナトリウ
ム濃度が処理液中の塩化ナトリウム濃度に保持される。
なお、塩水の電気分解により次亜塩素酸ナトリウムが生
成される場合に塩水中の塩化ナトリウムが消費されるが
その消費量は極めて少ないため、処理槽11に供給され
る次亜塩素酸ナトリウム含有する塩水中の塩化ナトリウ
ム濃度は処理液中の塩化ナトリウム濃度と略同じてあ
る。For this reason, the salt water in the first salt water storage tank 12a is supplied to the electrolytic tank 13, and the supplied salt water is electrolyzed to generate sodium hypochlorite in the salt water. Sodium chlorite is supplied to the treatment tank 11 together with the salt water, and the concentration of sodium hypochlorite in the treatment liquid is adjusted to a predetermined concentration to always maintain the sterilizing action. During this time, in the first salt water supply means 12, the salt water in the first salt water storage tank 12a is maintained at a predetermined water level by the action of the float switch 12f, the third concentration sensor 16f, the third controller 16c, and the like. The concentration is maintained at the concentration of sodium chloride in the processing solution.
In addition, when sodium hypochlorite is generated by the electrolysis of salt water, sodium chloride in the salt water is consumed, but the consumption amount is extremely small, so that sodium hypochlorite supplied to the treatment tank 11 is contained. The concentration of sodium chloride in the salt water is substantially the same as the concentration of sodium chloride in the treatment liquid.
【0023】また、食物の塩水処理において、処理液を
氷で急激に冷却したりまたは被処理食物が冷凍物である
場合には氷の溶解により処理液が希釈され、また被処理
食物から水分が浸出して処理液が希釈されることがあ
る。この状態が発生した場合には、第2コントローラ1
6bが第2濃度センサ16eからの検出信号に基づいて
第3開閉弁15eを開成して第2塩水収容槽15a内に
高濃度の塩化ナトリウムを含有する塩水を処理槽11に
供給して、処理液中の塩化ナトリウム濃度を所定の濃度
に調整する。In the treatment of food with salt water, the processing liquid is rapidly cooled with ice, or when the food to be processed is frozen, the processing liquid is diluted by melting of the ice, and water is removed from the food to be processed. Leaching may dilute the treatment liquid. When this state occurs, the second controller 1
6b opens the third on-off valve 15e based on the detection signal from the second concentration sensor 16e, and supplies the salt water containing high concentration sodium chloride into the second salt water storage tank 15a to the treatment tank 11 to perform the treatment. The concentration of sodium chloride in the solution is adjusted to a predetermined concentration.
【0024】このように、当該塩水処理装置10におい
ては、第1塩水収容槽12aから処理槽11内へ塩水を
供給して同処理槽11内に所定濃度の塩水からなる処理
液を収容することができるとともに、処理液が減少した
場合にはその都度第1塩水収容槽12aから処理槽11
へ塩水を供給して補うことができる。また、次亜塩素酸
ナトリウムは殺菌作用があるとともに塩水に対して十分
な量を溶解させることができるため、第1塩水収容槽1
2aから処理槽11への塩水の供給時に電解槽13の両
電極13a,13b間に電圧を印加して供給される塩水
を電解することができ、かつこの電解により塩水中に次
亜塩素酸ナトリウムを発生させて塩水とともに処理槽1
1内に供給することができる。As described above, in the salt water treatment apparatus 10, the salt water is supplied from the first salt water storage tank 12 a into the processing tank 11, and the processing liquid composed of the salt water having a predetermined concentration is stored in the processing tank 11. When the processing solution is reduced, the first salt water storage tank 12a and the processing tank 11
Can be supplemented by supplying salt water. Also, since sodium hypochlorite has a bactericidal action and can dissolve a sufficient amount in salt water, the first salt water storage tank 1
When the salt water is supplied from 2a to the treatment tank 11, a voltage is applied between the two electrodes 13a and 13b of the electrolytic tank 13 so that the supplied salt water can be electrolyzed. And treatment tank 1 with salt water
1 can be supplied.
【0025】このため、処理液中の次亜塩素酸ナトリウ
ムの濃度が所定の濃度より低下した場合等適宜の時点で
電解槽13を作動させて塩水を電解すれば、処理液を次
亜塩素酸ナトリウムに起因する殺菌作用を常時保持させ
ることができ、処理液中の雑菌を常に効果的に殺菌する
ことができる。この場合、処理液を殺菌するためにオゾ
ン、紫外線、その他の殺菌剤等を使用することがないた
め、オゾンの使用に起因する食物および装置等への汚
染、作業従事者の健康への影響、殺菌効果等の問題を解
消することができ、紫外線の使用に起因する殺菌効果の
問題、殺菌剤の使用に起因する殺菌効果および殺菌剤の
濃度管理等の問題を解消できる。For this reason, when the concentration of sodium hypochlorite in the treatment liquid falls below a predetermined concentration, for example, by operating the electrolytic cell 13 to electrolyze the salt water, the treatment liquid becomes hypochlorous acid. The bactericidal action caused by sodium can be always maintained, and germs in the processing solution can be constantly and effectively sterilized. In this case, ozone, ultraviolet rays, other disinfectants, etc. are not used to sterilize the processing solution, so that the use of ozone contaminates food and equipment, the effect on the health of workers, Problems such as a bactericidal effect can be solved, and problems such as a bactericidal effect due to the use of ultraviolet rays, a bactericidal effect due to the use of a bactericide, and a concentration control of a bactericide can be solved.
【0026】また、当該塩水処理装置10においては、
処理槽11内の処理液中の次亜塩素酸ナトリウム濃度を
検出しながら同濃度を調整する手段を採用しているた
め、処理液中の次亜塩素酸ナトリウム濃度を常に所定濃
度に自動的に調整することができる。また、第1塩水収
容槽12a内の塩水の塩化ナトリウム濃度を処理槽11
内の処理液中の塩化ナトリウム濃度と同一濃度に設定し
てるため、処理液中への次亜塩素酸ナトリウムの供給時
に処理液中の塩化ナトリウム濃度を変化させることがな
いという利点がある。In the salt water treatment apparatus 10,
Since the means for detecting and adjusting the sodium hypochlorite concentration in the processing liquid in the processing tank 11 is employed, the sodium hypochlorite concentration in the processing liquid is always automatically adjusted to a predetermined concentration. Can be adjusted. Further, the concentration of sodium chloride in the salt water in the first salt water storage tank 12a is determined by the treatment tank 11
Since the concentration is set to be the same as the concentration of sodium chloride in the processing solution, there is an advantage that the concentration of sodium chloride in the processing solution does not change when sodium hypochlorite is supplied to the processing solution.
【0027】図2には本発明の第2実施例に係る塩水処
理装置20が示されている。当該塩水処理装置20は処
理槽21、第1塩水供給手段22および電解槽23を備
えるとともに、処理水冷却手段24、第2塩水供給手段
25および制御手段26を備えている。これらにおい
て、処理槽21、第1塩水供給手段22、処理水冷却手
段24、第2塩水供給手段25および制御手段26は第
1実施例の塩水処理装置10と同様であり、電解槽23
が同塩水処理装置10の電解槽13とは相違し、またこ
れに起因して処理液の組成を異にする。FIG. 2 shows a salt water treatment apparatus 20 according to a second embodiment of the present invention. The salt water treatment apparatus 20 includes a treatment tank 21, a first salt water supply unit 22, and an electrolytic tank 23, and also includes a treated water cooling unit 24, a second salt water supply unit 25, and a control unit 26. In these, the treatment tank 21, the first salt water supply means 22, the treated water cooling means 24, the second salt water supply means 25, and the control means 26 are the same as those of the salt water treatment apparatus 10 of the first embodiment, and the electrolytic cell 23
Is different from the electrolytic cell 13 of the salt water treatment apparatus 10, and due to this, the composition of the treatment liquid is different.
【0028】電解槽23はケーシング内の陽極23aと
陰極23b間に隔膜23cを備えていて、隔膜23cに
よりケーシング内が陽極室23dと陰極23eとに区画
されている。かかる電解槽23においては、第1塩水収
容槽22aからの塩水が両室23d,23eにそれぞれ
別々に供給され、両室23d,23eに供給された塩水
は両電極23a,23bへの電圧の印加により電解され
て、陽極室23dにおいて次亜塩素酸が生成される。生
成された次亜塩素酸は塩水とともに処理槽21に供給さ
れる。従って、処理槽21内の処理液は所定濃度の次亜
塩素酸および塩化ナトリウムを含有する塩水であり、か
かる処理液においては次亜塩素酸が殺菌作用を行う。The electrolytic cell 23 has a diaphragm 23c between the anode 23a and the cathode 23b in the casing, and the casing is partitioned into an anode chamber 23d and a cathode 23e by the diaphragm 23c. In the electrolytic cell 23, the salt water from the first salt water storage tank 22a is separately supplied to the two chambers 23d and 23e, and the salt water supplied to the two chambers 23d and 23e is applied to the electrodes 23a and 23b. And hypochlorous acid is generated in the anode chamber 23d. The generated hypochlorous acid is supplied to the treatment tank 21 together with the salt water. Therefore, the processing liquid in the processing tank 21 is a salt water containing a predetermined concentration of hypochlorous acid and sodium chloride, and in such a processing liquid, hypochlorous acid performs a sterilizing action.
【0029】なお、当該塩水処理装置20についてのそ
の他の構成および作用効果は第1実施例の塩水処理装置
10と同様であり、従って塩水処理装置10と同一構成
の部分についてはその構成部材に20番台の類似する符
号を付与して、その詳細な説明を省略する。The other structure, operation and effect of the salt water treatment apparatus 20 are the same as those of the salt water treatment apparatus 10 of the first embodiment. Similar reference numerals are assigned to the series, and detailed descriptions thereof are omitted.
【図1】本発明の第1の発明の実施例に係る塩水処理装
置の概略構成図である。FIG. 1 is a schematic configuration diagram of a salt water treatment apparatus according to a first embodiment of the present invention.
【図2】本発明の第2の発明の実施例に係る塩水処理装
置の概略構成図である。FIG. 2 is a schematic configuration diagram of a salt water treatment apparatus according to a second embodiment of the present invention.
10,20…塩水処理装置、11,21…処理槽、1
2,22…第1塩水供給手段、12a,22a…第1塩
水収容槽、13,23…電解槽、13a,13b,23
a,23b…電極、23c…隔膜、14,24…処理水
冷却手段、15,25…第2塩水供給手段、15a,2
5a…第2塩水収容槽、16,26…制御手段。10, 20 ... salt water treatment device, 11, 21 ... treatment tank, 1
2, 22: first salt water supply means, 12a, 22a: first salt water storage tank, 13, 23: electrolytic tank, 13a, 13b, 23
a, 23b ... electrode, 23c ... diaphragm, 14, 24 ... treated water cooling means, 15, 25 ... second salt water supply means, 15a, 2
5a ... second salt water storage tank, 16, 26 ... control means.
Claims (4)
処理槽と、同処理槽へ供給する塩水を収容する塩水収容
槽と、同塩水収容槽の塩水を前記処理槽へ供給する供給
系路に配設され陽極および陰極間に供給された塩水を電
解して次亜塩素酸ナトリウムを生成する電解槽とを備え
たことを特徴とする食物の塩水処理装置。1. A processing tank for storing a processing solution composed of salt water having a predetermined concentration, a salt water storing tank for storing salt water to be supplied to the processing tank, and a supply system for supplying the salt water in the salt water storing tank to the processing tank. An electrolytic cell disposed on a road to electrolyze salt water supplied between an anode and a cathode to generate sodium hypochlorite.
処理槽と、同処理槽へ供給する塩水を収容する塩水収容
槽と、同塩水収容槽の塩水を前記処理槽へ供給する供給
系路に配設され陽極および陰極間に供給された塩水を電
解して次亜塩素酸を生成する電解槽とを備えたことを特
徴とする食物の塩水処理装置。2. A processing tank for storing a processing solution composed of salt water having a predetermined concentration, a salt water storing tank for storing salt water to be supplied to the processing tank, and a supply system for supplying the salt water in the salt water storing tank to the processing tank. An electrolyzer for producing hypochlorous acid by electrolyzing salt water supplied between an anode and a cathode, the apparatus being disposed on a road, and comprising an electrolytic tank.
理槽内の所定濃度の塩水からなる処理液の塩濃度と同一
である請求項1または2に記載の食物の塩水処理装置。3. The apparatus for treating salt water of food according to claim 1, wherein the salt concentration of the salt water in the salt water storage tank is the same as the salt concentration of the treatment liquid having a predetermined concentration in the treatment tank.
備えていることを特徴とする請求項1,2または3に記
載の食物の塩水処理装置。4. The apparatus for treating salt water of food according to claim 1, wherein said treatment tank is provided with cooling means for cooling the treatment liquid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32784291A JP2736578B2 (en) | 1991-12-11 | 1991-12-11 | Food salt water treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32784291A JP2736578B2 (en) | 1991-12-11 | 1991-12-11 | Food salt water treatment equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05161487A JPH05161487A (en) | 1993-06-29 |
JP2736578B2 true JP2736578B2 (en) | 1998-04-02 |
Family
ID=18203598
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32784291A Expired - Fee Related JP2736578B2 (en) | 1991-12-11 | 1991-12-11 | Food salt water treatment equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2736578B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5792343A (en) * | 1996-09-12 | 1998-08-11 | Hoshizaki Denki Kabushiki Kaisha | Brine supply system |
JP2002272435A (en) * | 2001-03-16 | 2002-09-24 | Hoshizaki Electric Co Ltd | Salt water-treating device |
DE102007020977A1 (en) * | 2007-05-04 | 2008-11-06 | Actides Gmbh | Process for treating food |
-
1991
- 1991-12-11 JP JP32784291A patent/JP2736578B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH05161487A (en) | 1993-06-29 |
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