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JPH0464658B2 - - Google Patents
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JPH0464658B2 - - Google Patents

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Publication number
JPH0464658B2
JPH0464658B2 JP60266611A JP26661185A JPH0464658B2 JP H0464658 B2 JPH0464658 B2 JP H0464658B2 JP 60266611 A JP60266611 A JP 60266611A JP 26661185 A JP26661185 A JP 26661185A JP H0464658 B2 JPH0464658 B2 JP H0464658B2
Authority
JP
Japan
Prior art keywords
water
cooling pipe
salt water
electrode
voltage
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
Application number
JP60266611A
Other languages
Japanese (ja)
Other versions
JPS62126963A (en
Inventor
Hideaki Kodate
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP60266611A priority Critical patent/JPS62126963A/en
Publication of JPS62126963A publication Critical patent/JPS62126963A/en
Publication of JPH0464658B2 publication Critical patent/JPH0464658B2/ja
Granted legal-status Critical Current

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  • Freezing, Cooling And Drying Of Foods (AREA)
  • Storage Of Fruits Or Vegetables (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)

Description

【発明の詳細な説明】 (イ) 産業上の利用分野 本発明は、肉、鮮魚等の食品を冷却塩水に浸漬
して冷却保存する冷塩水処理装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a cold brine treatment apparatus for cooling and preserving foods such as meat and fresh fish by immersing them in cool brine.

(ロ) 従来の技術 例えば実公昭56−12936号公報には、冷凍食品
を入れる水槽と冷却機とオゾン発生器とを備え、
水槽内の濾過槽の出口接続された管を吸水ポンプ
を経て冷却器の入口側へ導入し、この冷却機の出
口に接続された管の先端を水槽内に配置し、水槽
の底面にオゾンを発生するための気泡発生器を設
けた冷凍食品の解凍装置が示されている。
(b) Conventional technology For example, Japanese Utility Model Publication No. 56-12936 discloses a system equipped with a water tank for storing frozen food, a cooler, and an ozone generator.
Introduce the pipe connected to the outlet of the filtration tank inside the water tank to the inlet side of the cooler through the water suction pump, place the tip of the pipe connected to the outlet of the cooler inside the water tank, and apply ozone to the bottom of the tank. A device for defrosting frozen foods is shown which is provided with a bubble generator for generating bubbles.

(ハ) 発明が解決しようとする問題点 上記冷凍食品の解凍装置において、例えば魚又
は肉の切身等の凍結された食品を水槽内に浸した
場合には、氷が解けるにつれて水に対する浸透圧
の関係から前記水への肉汁の流出又は水の浸入に
よる酸化現象等が起り品質が劣化するため、前記
食品をビニール等の袋に入れて水槽内に投入する
必要があり、解凍作業は煩雑になる。又、前記問
題点を解決するために水槽内の水に食塩を溶かし
浸透圧を調整した際には、金属材からなる吸水ポ
ンプ、配管、水槽等に錆が発生しやすく、錆によ
る腐食が発生した場合には製品の寿命が短くなる
という問題点が発生していた。
(c) Problems to be solved by the invention In the above frozen food thawing apparatus, when frozen food such as fish or meat fillets is immersed in a water tank, the osmotic pressure of the water increases as the ice melts. As a result, oxidation phenomena occur due to the outflow of meat juices into the water or the ingress of water, resulting in deterioration of quality, so it is necessary to put the food into a plastic bag or the like and put it into the water tank, making the thawing process complicated. . In addition, when salt is dissolved in the water in the aquarium to adjust the osmotic pressure in order to solve the above problem, rust tends to form on the water suction pump, piping, aquarium, etc. made of metal materials, and corrosion due to rust occurs. In this case, a problem arises in that the life of the product is shortened.

(ニ) 問題点を解決するための手段 本発明は上記問題点を解決するために、塩水を
貯溜する貯水槽と、前記塩水を循環するポンプ
と、前記貯水槽内の塩水を冷却する冷却パイプ
と、該冷却パイプから離間して前記塩水に水没し
て設けられた電極と、該電極にプラス電圧を印加
する出力側のプラス端子、前記冷却パイプにマイ
ナス電圧を印加する入力側のマイナス端子を備
え、前記電極から前記塩水を介して前記冷却パイ
プへ定電流を流す定電流発生回路と、前記プラス
端子の電圧とマイナス端子の電圧とを比較して前
記ポンプの運転を停止する渇水検出信号を出力す
る比較器とを備えたことを特徴とする冷塩水処理
装置を提供するものである。
(d) Means for Solving the Problems In order to solve the above problems, the present invention provides a water storage tank for storing salt water, a pump for circulating the salt water, and a cooling pipe for cooling the salt water in the water storage tank. an electrode provided apart from the cooling pipe and submerged in the salt water; a positive terminal on the output side for applying a positive voltage to the electrode; and a negative terminal on the input side for applying a negative voltage to the cooling pipe. a constant current generating circuit that flows a constant current from the electrode to the cooling pipe through the salt water; and a water shortage detection signal that compares the voltage of the positive terminal and the voltage of the negative terminal to stop operation of the pump. The present invention provides a cold salt water treatment device characterized by comprising a comparator for outputting the cold salt water.

(ホ) 作 用 水槽内に所定濃度の塩水を満たし、この水槽内
に肉、魚の食品を収納して冷却保存するとき、各
食品の浸透圧が異なるために種々の食品に合わせ
て浸透圧を調整する必要があり、このため、塩水
の濃度を浸漬食品を変更する毎に変えるために、
塩水の伝導率は変化する。しかし乍ら、定電流回
路のプラス端子に接続された電極から、塩水を介
して前記定電流回路のマイナス端子に接続された
冷却パイプへ前記電流伝導率の変化に関係なく一
定電流が流れる。又、貯水槽内の塩水が抜けて電
極が空気に晒された場合には、プラス端子の電圧
とマイナス端子の電圧との差がゼロとなつて比較
器から渇水検出信号が出力されてポンプの運転が
停止される。
(E) Function When filling an aquarium with salt water of a predetermined concentration and storing meat and fish foods in this aquarium for cooling preservation, each food has a different osmotic pressure, so the osmotic pressure must be adjusted to suit the various foods. For this reason, it is necessary to adjust the concentration of the brine to change each time you change the soaked food.
The conductivity of salt water varies. However, a constant current flows from the electrode connected to the positive terminal of the constant current circuit to the cooling pipe connected to the negative terminal of the constant current circuit via the salt water, regardless of the change in the current conductivity. Additionally, if the salt water in the water storage tank is drained and the electrode is exposed to air, the difference between the voltage at the positive terminal and the voltage at the negative terminal becomes zero, and the comparator outputs a water shortage detection signal, causing the pump to Operation will be stopped.

(ヘ) 実施例 以下、本発明の一実施例を図面に基づいて詳細
に説明する。第2図は本冷塩水処理装置1の側面
図、第3図は同平面図を示している。2は上方に
開放した断熱箱にて画成される貯水槽で、内部に
は仕切板3によつて左右に主水槽4及び副水槽5
が区画形成されている。主水槽4内には食品が収
納される為下部に網棚6が設置される。副水槽5
内には仕切板3の上端より下方に於いて水平に濾
過器としてのスクリーン7が架設され、更にその
下方に冷却装置9の冷凍サイクルに含まれる冷却
パイプ8が貯水槽2の底部から離間して配置され
る。更に副水槽5上方の貯水槽2開口部には水切
り台10が架設される。12は冷却装置の冷凍サ
イクルを構成する電動圧縮機13や凝縮器14、
そしてオゾン発生装置から成る殺菌装置15を収
納するユニツト箱体であり、副水槽5側の貯水槽
2側部に配置され、冷却パイプ8はそこから副水
槽5内に延在しており、更に箱体12の上面は平
面としてその高さは水切り台10と同じ高さとし
ている。これによつて箱体12上面はテーブルと
して使用可能となつている。又、水切り台10が
副水槽5上にあるので、冷却、洗浄或いは解凍処
理後の食品17の水切りが非常に容易となる。
(F) Embodiment Hereinafter, an embodiment of the present invention will be described in detail based on the drawings. FIG. 2 shows a side view of the cold salt water treatment apparatus 1, and FIG. 3 shows a plan view thereof. Reference numeral 2 denotes a water storage tank defined by an insulated box that opens upward, and inside there are a main water tank 4 and a sub-water tank 5 on the left and right sides separated by a partition plate 3.
are divided into sections. A net shelf 6 is installed at the bottom of the main water tank 4 to store food. Sub-tank 5
Inside, a screen 7 as a filter is installed horizontally below the upper end of the partition plate 3, and further below the screen 7, a cooling pipe 8 included in the refrigeration cycle of the cooling device 9 is spaced apart from the bottom of the water storage tank 2. will be placed. Further, a draining table 10 is installed at the opening of the water tank 2 above the sub-water tank 5. 12 is an electric compressor 13 and a condenser 14 that constitute the refrigeration cycle of the cooling device;
It is a unit box that houses a sterilizer 15 consisting of an ozone generator, and is arranged on the side of the water tank 2 on the side of the sub-water tank 5, from which the cooling pipe 8 extends into the sub-water tank 5. The upper surface of the box body 12 is a flat surface, and its height is the same as that of the draining stand 10. This allows the top surface of the box 12 to be used as a table. Further, since the draining table 10 is located on the sub-water tank 5, it is very easy to drain the food 17 after cooling, washing, or thawing.

貯水槽2内に注入される塩水18には収納する
食品が肉或いは鮮魚の場合には浸透圧を調節する
為に食塩が混入されており、肉では約1%、鮮魚
では3.5%の食塩水とされる。塩水18は箱体1
2内に設置した後述するポンプ19により副水槽
5底部に開口した吸入管20より吸入され、殺菌
装置15によつて殺菌された後、主水槽4底部に
開口した吐出管21より主水槽4内に吐出され
る。主水槽4内の水位は予め仕切板3の高さを越
えるものとされ、これによつてオーバーフローし
た塩水18はスクリーン7により濾過されて副水
槽5内に落下し貯溜され、再び吸入管20より吸
い込まれる循環をする。この時副水槽5内の水位
は冷却パイプ20より上方にある様にし、これに
よつて水は冷却され、野菜では例えば+5℃、肉
では0℃、鮮魚では−2℃とされる。斯かる食品
は主水槽4内に於いて冷水により冷却されること
によりその芯温の冷却速度が速くなる効果があ
る。又、食品の洗浄に使用する場合にもスクリー
ン7によつてゴミは濾過されるのでポンプ19等
の目詰りが生じない。
When the food to be stored is meat or fresh fish, the salt water 18 injected into the water storage tank 2 is mixed with salt to adjust the osmotic pressure, and the salt water is about 1% for meat and 3.5% for fresh fish. It is said that Salt water 18 is box body 1
The pump 19, which will be described later, is installed in the tank 2, and the suction pipe 20 opens at the bottom of the sub-tank 5. After being sterilized by the sterilizer 15, the water is sucked into the main tank 4 through the discharge pipe 21 opened at the bottom of the main tank 4. is discharged. The water level in the main water tank 4 is set to exceed the height of the partition plate 3 in advance, so that the overflowing salt water 18 is filtered by the screen 7 and falls into the sub water tank 5 to be stored there, and is then returned to the suction pipe 20. It goes through a cycle of being sucked in. At this time, the water level in the sub-tank 5 is set above the cooling pipe 20, thereby cooling the water to, for example, +5°C for vegetables, 0°C for meat, and -2°C for fresh fish. Such foods are cooled by cold water in the main water tank 4, which has the effect of increasing the cooling rate of their core temperatures. Further, even when used for washing food, since the screen 7 filters out dirt, the pump 19 etc. will not be clogged.

前記塩水18には食品の臭いやスクリーン7で
濾過されなかつた細かい屑が混ざるため、取り替
える必要があり、そのため本願では第4図に示す
如く吸入管20にポンプ19方向に向う導管51
つり分岐する導管51を設け、この導管52の途
中には常閉の弁53を取り付ける。即ち、塩水1
8を廃棄する場合には仕切板3を取り外して主水
槽4と副水槽5を連通せしめた状態で弁53を開
けば貯水槽2内の水18は吸入管20及び導管5
2を流下してその排出口54より排出せられる。
又、この時吐出管21を導管51,52等より上
方に位置せしめてあるから、吐出管21内の水1
8もポンプ19及び導管51を逆流して排出口5
4より排出されるので、各配管内の汚水も良好に
排出できる。
Since the salt water 18 contains food odors and fine particles that have not been filtered through the screen 7, it needs to be replaced. Therefore, in the present invention, as shown in FIG.
A conduit 51 that is suspended and branched is provided, and a normally closed valve 53 is installed in the middle of this conduit 52. That is, salt water 1
8, remove the partition plate 3 and open the valve 53 to communicate the main water tank 4 and the sub-water tank 5.
2 flows down and is discharged from the discharge port 54.
Also, since the discharge pipe 21 is positioned above the conduits 51, 52, etc. at this time, the water 1 in the discharge pipe 21 is
8 also flows back through the pump 19 and the conduit 51 to the discharge port 5.
4, the wastewater inside each pipe can also be drained well.

前記冷却パイプ8は銅、ニツケル合金からな
り、第1図に示す如くその適所にリード線30が
接続されている。又31は前記銅、ニツケル合金
よりも更に防食性に優れた例えばチタンからなる
電極で、冷却パイプ8から離間すると共に、その
下端が冷却パイプ8の下部と略同じ高さになるよ
うに配置されている。
The cooling pipe 8 is made of copper or nickel alloy, and lead wires 30 are connected to appropriate positions thereof as shown in FIG. Reference numeral 31 denotes an electrode made of, for example, titanium, which has better corrosion resistance than the copper or nickel alloy, and is spaced apart from the cooling pipe 8 and arranged so that its lower end is approximately at the same height as the lower part of the cooling pipe 8. ing.

又、第1図の40は定電流回路で、この定電流
回路は直流電源ライン41,42間に直列接続さ
れた第1抵抗R1と第2抵抗R2との直列回路と、
この直列回路の中点がプラス側入力端子に接続さ
れた増幅器43と、この増幅器43のマイナス側
入力端子の入力電圧を決める第3抵抗R3と、増
幅器43の出力端子に第4抵抗R4を介して接続
されたNPN型トランジスタ44とから構成され
ている。ここでトランジスタ44のエミツタはプ
ラス端子45を介して陽極になりプラス電圧が印
加される電極31に接続され、増幅器43のマイ
ナス側入力端子はマイナス端子46を介して陰極
になる冷却パイプ8に探続されている。又、47
は比較器で、R5,R6及びR7は夫々第5、第6及
び第7抵抗である。尚、比較器47のマイナス側
入力端子は増幅器43のマイナス側入力端子に接
続されている。
Further, 40 in FIG. 1 is a constant current circuit, and this constant current circuit includes a series circuit of a first resistor R 1 and a second resistor R 2 connected in series between the DC power supply lines 41 and 42;
An amplifier 43 whose midpoint of this series circuit is connected to the positive input terminal, a third resistor R 3 that determines the input voltage of the negative input terminal of this amplifier 43, and a fourth resistor R 4 connected to the output terminal of the amplifier 43. The NPN type transistor 44 is connected through the NPN type transistor 44. Here, the emitter of the transistor 44 becomes an anode through a positive terminal 45 and is connected to the electrode 31 to which a positive voltage is applied, and the negative input terminal of the amplifier 43 is connected to the cooling pipe 8 which becomes a cathode through a negative terminal 46. It is continued. Also, 47
is a comparator, and R 5 , R 6 and R 7 are the fifth, sixth and seventh resistors, respectively. Note that the negative input terminal of the comparator 47 is connected to the negative input terminal of the amplifier 43.

上記直流電源ライン41,42間に直流電力を
与えると、定電流回路40のプラス端子45から
電極31、導電体になる塩水18、被防食体であ
る冷却パイプ8を介してマイナス端子46へ防食
に必要な例えば30mAの微弱な直流電流が流れ
る。この結果、陽極部となる電極31と陰極部と
なる冷却パイプ8との電位差(エネルギー差)を
消滅させて、冷却パイプ8の溶解反応を回避した
電気防食が行われる。即ち、陰極部になる冷却パ
イプ8の表面に微弱な直流電流を流入させ、これ
により、腐食電池を消滅させる電気防食法によ
り、冷却パイプ8の腐食を防止できる。ここで、
腐食電池は金属表面に局部的に発生する腐食の原
因になるものである。
When DC power is applied between the DC power lines 41 and 42, it is transmitted from the positive terminal 45 of the constant current circuit 40 to the negative terminal 46 via the electrode 31, the salt water 18 which becomes a conductor, and the cooling pipe 8 which is the object to be protected against corrosion. For example, a weak direct current of 30 mA, which is necessary for this purpose, flows. As a result, the potential difference (energy difference) between the electrode 31 serving as the anode portion and the cooling pipe 8 serving as the cathode portion is eliminated, and cathodic protection is performed in which a dissolution reaction of the cooling pipe 8 is avoided. That is, corrosion of the cooling pipe 8 can be prevented by a cathodic protection method in which a weak direct current is caused to flow into the surface of the cooling pipe 8, which becomes the cathode portion, thereby extinguishing the corroded battery. here,
Corrosion batteries cause localized corrosion on metal surfaces.

又、上記定電流回路40において、直流電源ラ
イン41,42間に電源電圧VCが与えられ、増
幅器43のプラス入力端子の基準電位をVP、定
電流回路40のプラス入力端子45からの防食出
力電流をI0、第1、第2及び第3抵抗R1,R2
びR3の抵抗値を夫々符号と等しいR1,R2及びR3
とすると、 VP=VC/(R1/R2+1) I0≒VP/R3 にて表わされ、増幅器43の出力端子から第4抵
抗R4を通してトランジスタ44にバイアスされ
る。このバイアスによりプラス端子45から防食
出力電流I0が流れ、増幅器43はマイナス側入力
端子の電位がプラス側入力端子の電位と等しくな
るように出力し、バイアス電圧を変化させる。
Further, in the constant current circuit 40, a power supply voltage V C is applied between the DC power supply lines 41 and 42, the reference potential of the positive input terminal of the amplifier 43 is set to V P , and a corrosion protection voltage from the positive input terminal 45 of the constant current circuit 40 is applied. The output current is I 0 and the resistance values of the first, second and third resistors R 1 , R 2 and R 3 are equal to the sign R 1 , R 2 and R 3 respectively.
Then, it is expressed as V P =V C /(R 1 /R 2 +1) I 0 ≈V P /R 3 and is biased from the output terminal of the amplifier 43 to the transistor 44 through the fourth resistor R 4 . Due to this bias, the anticorrosion output current I 0 flows from the positive terminal 45, and the amplifier 43 outputs an output so that the potential of the negative input terminal becomes equal to the potential of the positive input terminal, thereby changing the bias voltage.

尚、定電流回路40の防食出力電流I0は、冷却
パイプ8の塩水に水没している部分の表面積及び
材質、電極31の長さ、冷却パイプ8と電極31
との距離等により決まるものである。そして、冷
却パイプ8の前記表面積が略4.5m2、材質が銅と
ニツケルとの合金、電極31の長さが略20cm、冷
却パイプ8と電極31との距離が略20cmのときは
防食出力電流I0を30mAに設定することにより、
冷却パイプ8の防食を図ることができる。
The anti-corrosion output current I0 of the constant current circuit 40 depends on the surface area and material of the portion of the cooling pipe 8 submerged in salt water, the length of the electrode 31, and the length of the cooling pipe 8 and the electrode 31.
This is determined by the distance from the When the surface area of the cooling pipe 8 is approximately 4.5 m 2 , the material is an alloy of copper and nickel, the length of the electrode 31 is approximately 20 cm, and the distance between the cooling pipe 8 and the electrode 31 is approximately 20 cm, the anticorrosion output current is By setting I 0 to 30mA,
Corrosion prevention of the cooling pipe 8 can be achieved.

ここで、貯水槽2内に例えば肉を収納するため
に水を給水して塩水18の濃度を低下させて約1
%にしたときには、濃度が低いために塩水18の
伝導率は低下する。そして、前記伝導率が低下し
たときには、電極31から冷却パイプ8へ電流が
流れにくくなり、第3抵抗R3を流れる電流即ち
定電流回路40の出力電流I0は低下して、第3抵
抗R3の端子電圧は低下する。第3抵抗R3の端子
電圧が低下すると、増幅器43のマイナス側入力
電圧も低下して増幅器43の出力電圧は上昇す
る。このため、トランジスタ44のバイアスは大
きくなり、定電流回路40の出力電流I0は低下し
た分増加して電極31から冷却パイプ8へ流れる
電流は伝導率が変化する前と略等しくなる。
Here, water is supplied into the water storage tank 2 to store meat, for example, and the concentration of the salt water 18 is reduced to about 1
%, the conductivity of the salt water 18 decreases due to its low concentration. When the conductivity decreases, it becomes difficult for the current to flow from the electrode 31 to the cooling pipe 8, and the current flowing through the third resistor R3 , that is, the output current I0 of the constant current circuit 40 decreases, and the third resistor R3 decreases. 3 terminal voltage decreases. When the terminal voltage of the third resistor R 3 decreases, the negative input voltage of the amplifier 43 also decreases, and the output voltage of the amplifier 43 increases. Therefore, the bias of the transistor 44 increases, the output current I 0 of the constant current circuit 40 increases by the amount of the decrease, and the current flowing from the electrode 31 to the cooling pipe 8 becomes approximately equal to that before the conductivity changed.

又、貯水槽2内に例えば鮮魚を収納するため
に、槽内に塩を供給して塩水18の濃度を上昇さ
せて約3.5%にしたときには、濃度が上昇したた
めに塩水18の伝導率は上昇する。そして、伝導
率が上昇したときには、電極31から冷却パイプ
8へ電流が流れやすくなる。従つて、第3抵抗
R3を流れる電流即ち出力電流I0は上昇して、第3
抵抗R3の端子電圧は上昇する。第3抵抗R3の端
子電圧が上昇すると、増幅器43のマイナス側入
力電圧も上昇して、増幅器43の出力電圧は降下
する。このため、トランジスタ44のバイアスは
小さくなり、定電流回路40の出力電流I0は上昇
した分低下して電極31から冷却パイプ8へ流れ
る電流は伝導率が変化する前と略等しくなる。
Furthermore, when, for example, fresh fish is stored in the water storage tank 2, salt is supplied into the tank to increase the concentration of the salt water 18 to approximately 3.5%, the conductivity of the salt water 18 increases due to the increased concentration. do. When the conductivity increases, current flows more easily from the electrode 31 to the cooling pipe 8. Therefore, the third resistor
The current flowing through R 3 , that is, the output current I 0 increases, and the third
The terminal voltage of resistor R 3 increases. When the terminal voltage of the third resistor R 3 increases, the negative input voltage of the amplifier 43 also increases, and the output voltage of the amplifier 43 decreases. Therefore, the bias of the transistor 44 becomes smaller, the output current I 0 of the constant current circuit 40 decreases by the increased amount, and the current flowing from the electrode 31 to the cooling pipe 8 becomes approximately equal to that before the conductivity changed.

さらに、貯水槽2内の塩水18に電極31及び
冷却パイプ8が水没しているときは、比較器47
のマイナス側入力電圧は第3抵抗R3の端子電圧
と等しく、プラス側入力電圧より常に高いため、
比較器47はローレベル信号を出力して渇水検出
信号を出力しない。このとき、例えば弁53の故
障により、貯水槽2の塩水18が徐々に抜け、電
極31が水面から離れた場合には、電極31と冷
却パイプ8との間、即ちプラス端子45とマイナ
ス端子46との間がオープンになる。従つて、比
較器47のマイナス入力電圧はゼロVになり、比
較器47は渇水検出信号であるハイレベル信号を
出力し、ブザー等の渇水警報装置(図示せず)が
動作する。又、渇水検出信号によりポンプ19の
運転は停止される。
Furthermore, when the electrode 31 and the cooling pipe 8 are submerged in the salt water 18 in the water storage tank 2, the comparator 47
The negative input voltage of is equal to the terminal voltage of the third resistor R3 , which is always higher than the positive input voltage, so
The comparator 47 outputs a low level signal and does not output a drought detection signal. At this time, if the salt water 18 in the water storage tank 2 gradually escapes and the electrode 31 leaves the water surface due to a failure of the valve 53, for example, the gap between the electrode 31 and the cooling pipe 8, that is, the positive terminal 45 and the negative terminal 46 The gap between them becomes open. Therefore, the negative input voltage of the comparator 47 becomes zero V, the comparator 47 outputs a high level signal which is a drought detection signal, and a drought warning device (not shown) such as a buzzer operates. Further, the operation of the pump 19 is stopped by the water shortage detection signal.

従つて、冷却パイプ8及びこの冷却パイプから
離間して設けられた電極31が共に貯水槽2の塩
水18に水没されている状態のときには、塩水1
8を導電体として電極31から冷却パイプ8に向
けて微弱な直流電流が流れ、この結果、陽極部と
なる電極31と陰極部となる冷却パイプ8との電
位差(エネルギー差)を消滅させ、冷却パイプ8
の溶解反応を回避した電気防食が行える。即ち、
冷却パイプ8そのものを定電流回路40のマイナ
ス端子46に接続して陰極として兼用させること
により、導電体且つ電解質となる塩水18を通し
て微弱な直流電流を冷却パイプ8の表面に流入さ
せ、これにより腐食電池を消滅させる電気化学的
防食法を採用して冷却パイプ8の腐食を防止でき
る。
Therefore, when the cooling pipe 8 and the electrode 31 provided apart from the cooling pipe are both submerged in the salt water 18 in the water storage tank 2, the salt water 1
8 as a conductor, a weak direct current flows from the electrode 31 toward the cooling pipe 8, and as a result, the potential difference (energy difference) between the electrode 31, which becomes the anode part, and the cooling pipe 8, which becomes the cathode part, disappears, and cooling is performed. pipe 8
Electrolytic protection can be achieved while avoiding the dissolution reaction. That is,
By connecting the cooling pipe 8 itself to the negative terminal 46 of the constant current circuit 40 and making it double as a cathode, a weak direct current flows into the surface of the cooling pipe 8 through the salt water 18 that serves as a conductor and electrolyte, thereby preventing corrosion. Corrosion of the cooling pipe 8 can be prevented by employing an electrochemical corrosion protection method that eliminates the battery.

又、電極31は冷却パイプ8よりも防食性に優
れた金属材よりなるものであるから、電極31の
腐食の速さは遅いのは勿論、貯水槽2内の塩水1
8の濃度を濃くして塩水18の伝導率が高くなつ
た場合には、定電流回路40は出力電流I0が上昇
しないように作用して、濃度の変化前と等しい電
流が電極31から冷却パイプ8へ流れるため、電
極31の金属イオンの電気分解は略一定で、腐食
が速く進むことはなく、この結果、電極31を長
期間にわたり使用することができ、又、出力電流
I0を一定に保ち消費電力の削減を図ることができ
る。
In addition, since the electrode 31 is made of a metal material that has better corrosion resistance than the cooling pipe 8, the corrosion rate of the electrode 31 is slow, and the salt water 1 in the water storage tank 2
When the conductivity of the salt water 18 increases by increasing the concentration of the salt water 8, the constant current circuit 40 acts so that the output current I0 does not increase, and the same current as before the concentration change flows from the electrode 31 for cooling. Because it flows into the pipe 8, the electrolysis of metal ions in the electrode 31 is approximately constant, and corrosion does not proceed rapidly. As a result, the electrode 31 can be used for a long period of time, and the output current
It is possible to keep I 0 constant and reduce power consumption.

さらに、塩水18の濃度を薄くして塩水18の
伝導率が低くなつた場合には、定電流回路40は
出力電流I0が低下しないように作用して、濃度の
変化前と等しい防食に必要な電流が電極31から
冷却パイプ8へ流れるため、濃度が低下しても腐
食電池を消滅させて確実に冷却パイプ8の腐食を
防止できる。
Furthermore, when the conductivity of the salt water 18 decreases by diluting the concentration of the salt water 18, the constant current circuit 40 acts to prevent the output current I0 from decreasing, which is necessary for corrosion protection equal to that before the concentration change. Since a current flows from the electrode 31 to the cooling pipe 8, even if the concentration decreases, the corrosion battery can be extinguished and corrosion of the cooling pipe 8 can be reliably prevented.

尚、本発明に係る定電流回路は上記実施例にて
説明した定電流回路40に限定されるものではな
く、塩水18の伝導率の変化に対応して動作して
電極31と冷却パイプ8との間に常に定電流を流
す回路であれば良い。
Note that the constant current circuit according to the present invention is not limited to the constant current circuit 40 described in the above embodiment, and operates in response to changes in the conductivity of the salt water 18 to connect the electrode 31 and the cooling pipe 8. It is sufficient if the circuit always flows a constant current between the two.

(ト) 発明の効果 本発明は上記実施例にて説明した冷塩水処理装
置であるから、貯水槽内に貯えられた塩水を冷却
する冷却パイプを定電流回路のマイナス端子に接
続し、この冷却パイプから離間して前記塩水に水
没される電極を前記定電流回路のプラス端子に接
続することにより、前記冷却パイプそのものを陰
極として使用することができ、この結果、前記定
電流回路から出力された直流電流を導電体となる
前記塩水を通して前記電極から前記冷却パイプへ
流して、該冷却パイプの防食を図ることができる
のは勿論、前記貯水槽内へ収納する食品の種類に
対応して塩水の濃度を変え、そのため前記塩水の
伝導率が変化した場合にも、前記定電流回路から
常に一定の電流が出力され、前記電極から前記冷
却パイプへ常に一定の電流が流れるため、前記電
極の金属イオンの電気分解速度は極めて遅く、食
塩を入れても腐食が速く進むことはなく、この結
果、前記電極を長期間にわたり使用することがで
き、又、前記電極から前記冷却パイプへ流れる電
流を一定に保ち消費電力の削減を図ることがで
き、又、塩水の濃度が薄いため伝導率が低いとき
には、前記定電流回路は出力電流が低下しないよ
うに作用して、濃度の変化に関係なく等しい電流
が電極から冷却パイプへ流れるため、濃度が低下
しても腐食電池を消滅させて確実に冷却パイプの
腐食を防止できる。又、貯水槽内の塩水が抜けて
電極が空気に晒された場合には、プラス端子の電
圧とマイナス端子の電圧との差がゼロとなつて比
較器から渇水検出信号が出力されてポンプの運転
が停止される関係上、排水弁の故障や配水管の破
損等で塩水が貯水槽から漏れた場合におけるポン
プの保護が行える。
(G) Effects of the Invention Since the present invention is the cold salt water treatment apparatus explained in the above embodiment, the cooling pipe for cooling the salt water stored in the water storage tank is connected to the negative terminal of the constant current circuit, and the cooling pipe is connected to the negative terminal of the constant current circuit. By connecting an electrode separated from the pipe and submerged in the salt water to the positive terminal of the constant current circuit, the cooling pipe itself can be used as a cathode, so that the output from the constant current circuit Of course, it is possible to prevent corrosion of the cooling pipe by flowing direct current from the electrode to the cooling pipe through the salt water, which serves as a conductor. Even if the concentration changes and therefore the conductivity of the salt water changes, a constant current is always output from the constant current circuit, and a constant current always flows from the electrode to the cooling pipe, so that the metal ions of the electrode The rate of electrolysis of is extremely slow, and even if salt is added, corrosion will not proceed rapidly.As a result, the electrode can be used for a long period of time, and the current flowing from the electrode to the cooling pipe can be kept constant. In addition, when the conductivity is low due to the low concentration of salt water, the constant current circuit acts to prevent the output current from decreasing, so that the same current is maintained regardless of changes in concentration. Since it flows from the electrode to the cooling pipe, even if the concentration decreases, corrosion batteries can be extinguished and corrosion of the cooling pipe can be reliably prevented. Additionally, if the salt water in the water storage tank is drained and the electrode is exposed to air, the difference between the voltage at the positive terminal and the voltage at the negative terminal becomes zero, and the comparator outputs a water shortage detection signal, causing the pump to Since operation is stopped, the pump can be protected in the event that salt water leaks from the water tank due to a malfunction of the drain valve or damage to the water pipe.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図乃至第4図は本発明の一実施例を示し、
第1図は冷塩水処理装置の概略電気回路及び部分
縦断面図、第2図は冷塩水処理装置の側面図、第
3図は同平面図、第4図は貯水槽の断面図であ
る。 2…貯水槽、8…冷却パイプ、18…塩水、3
1…電極、40…定電流回路、45…プラス端
子、46…マイナス端子。
1 to 4 show an embodiment of the present invention,
FIG. 1 is a schematic electric circuit and a partial vertical sectional view of the cold salt water treatment device, FIG. 2 is a side view of the cold salt water treatment device, FIG. 3 is a plan view thereof, and FIG. 4 is a sectional view of a water storage tank. 2...Water tank, 8...Cooling pipe, 18...Salt water, 3
1... Electrode, 40... Constant current circuit, 45... Plus terminal, 46... Minus terminal.

Claims (1)

【特許請求の範囲】[Claims] 1 塩水を貯溜する貯水槽と、前記塩水を循環す
るポンプと、前記貯水槽内の塩水を冷却する冷却
パイプと、該冷却パイプから離間して前記塩水に
水没して設けられた電極と、該電極にプラス電圧
を印加する出力側のプラス端子、前記冷却パイプ
にマイナス電圧を印加する入力側のマイナス端子
を備え、前記電極から前記塩水を介して前記冷却
パイプへ定電流を流す定電流発生回路と、前記プ
ラス端子の電圧とマイナス端子の電圧とを比較し
て前記ポンプの運転を停止する渇水検出信号を出
力する比較器とを備えたことを特徴とする冷塩水
処理装置。
1. A water storage tank for storing salt water, a pump for circulating the salt water, a cooling pipe for cooling the salt water in the water storage tank, an electrode provided apart from the cooling pipe and submerged in the salt water, A constant current generating circuit that includes a positive terminal on the output side for applying a positive voltage to the electrode and a negative terminal on the input side for applying a negative voltage to the cooling pipe, and that flows a constant current from the electrode to the cooling pipe via the salt water. and a comparator that compares the voltage at the positive terminal and the voltage at the negative terminal and outputs a water shortage detection signal for stopping operation of the pump.
JP60266611A 1985-11-26 1985-11-26 Cold salt water treating apparatus Granted JPS62126963A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60266611A JPS62126963A (en) 1985-11-26 1985-11-26 Cold salt water treating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60266611A JPS62126963A (en) 1985-11-26 1985-11-26 Cold salt water treating apparatus

Publications (2)

Publication Number Publication Date
JPS62126963A JPS62126963A (en) 1987-06-09
JPH0464658B2 true JPH0464658B2 (en) 1992-10-15

Family

ID=17433220

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60266611A Granted JPS62126963A (en) 1985-11-26 1985-11-26 Cold salt water treating apparatus

Country Status (1)

Country Link
JP (1) JPS62126963A (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54158815U (en) * 1978-04-28 1979-11-06
JPS5948633A (en) * 1982-09-11 1984-03-19 Shimadzu Corp Material tester

Also Published As

Publication number Publication date
JPS62126963A (en) 1987-06-09

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