JP3641752B2 - Electrolyzed water generator - Google Patents

Electrolyzed water generator Download PDF

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Publication number
JP3641752B2
JP3641752B2 JP30698894A JP30698894A JP3641752B2 JP 3641752 B2 JP3641752 B2 JP 3641752B2 JP 30698894 A JP30698894 A JP 30698894A JP 30698894 A JP30698894 A JP 30698894A JP 3641752 B2 JP3641752 B2 JP 3641752B2
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Prior art keywords
water
electrolytic cell
electrolyte
backwashing
anode
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JPH08141569A (en
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啓治 柿沼
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日本インテック株式会社
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Description

【0001】
【産業上の利用分野】
この発明は、水道水を原水として使用する電解水生成装置の陽極室から吐出する陽極水を主に使用する装置に関するものである。更に詳述すると、このような装置の電解槽の陰極室上部および陰極室吐出管の付着物洗浄と陽極室吐出管に付設したORP電極の保護に関するものである。
【0002】
【従来の技術】
図2に示す電解水生成装置において、電解槽1は、電解槽内を隔膜2によって陰極室3と陽極室4に分け、夫夫の室内に電極5、6を挿入し、水道水などの原水をバルブ8をもって開閉自在に流入し、給水管10に電解質供給槽9から電解質を所定量添加した後、給水管10から分岐した給水管11、12をもって陰陽極室に給水する。陰陽極室内に供給した水道水などの原水を電極間に印加した直流電流7の通電によって電気分解することにより陰極室に陰極水を、陽極室に陽極水を電解生成するものである。電解された陰陽極水は夫夫の吐出管13、14から吐水する。陽極水吐出管14には吐出した陽極水の能力を確認するORP計の電極15が設置してある。
【0003】
電解槽供給前の原水中に電解質としてNaCl、KClなどのハロゲン化合物を一定の割合で添加して、電解槽で電気分解すると、電解質を構成するアニオンは陽極室に移動する。この結果、陽極室にはHClO、ClO-など、消毒および殺菌効果のあるアニオンを多量に含んだ低いpHの陽極水が得られる。この水には消毒および殺菌効果があるため、消毒および殺菌用洗浄用水として使用される。
【0004】
ところがこのような陽極水を主に得る装置においては陽極水に伴生して極めてpHの高い陰極水が吐出する。水道水などの原水中にはCaイオンが存在するがCaイオンは高いpHの領域で炭酸カルシウムや水酸化カルシウムとなって沈殿し、次第に電解槽の上部や吐出管路などを閉塞する。
【0005】
このため、一定時間の吐水ごとに電解質の電解槽への流入を止めると共に、陰陽極に印加する電圧の方向を逆転する逆洗をして、陰電極や陰極室中の陰極水に析出する上記カルシウム塩を洗浄し、溶解させることが行われている。この結果、付着した炭酸カルシウムや水酸化カルシウムは溶解する。ところがこの方法で上記の洗浄を行っても陰極室上部近傍の電解電流密度の小さい領域や陰極吐出管などは十分に逆洗されず、洗浄効果がでにくい面がある。また、洗浄を逆洗のみで行おうとすると長時間の逆洗をしなければならず、この間の電解電流に無駄が生じる。
【0006】
逆洗の際、陽極室から吐水する陰極水は高いpHのアルカリ性を示す。陽極室吐水管に配設されたORP計は低いpHの酸性水の酸化還元電位を測るための装置であり、これに適合する電極構造に形成されているので、高いpHのアルカリ水に一旦触れるとその後正確な値を示さなくなったり、正確な値を示すまでに長時間を要することとなる。陽極水使用者は陽極水の能力をORP計の表示に従って判断する。上記のように、逆洗が終わって通常の陽極水が流れても暫くの間はORP計の表示が正しくないとすると、陽極水使用者はその間の吐水を排水することになる。ところが、陽極水そのものはORPの表示が正しくないだけで、実際は能力のある状態で吐水されている可能性があり、その間の排水は無駄になる。
【0007】
【発明が解決しようとする課題】
そこで本発明は、陽極水を主に使用する装置において、電解質供給槽と電解槽との間に薬液添加槽を設けると共に、薬液添加槽に有機酸からなる薬剤を収納して、上記逆洗中は少なくとも原水に電解質を添加しながら、原水に上記薬剤を添加して供給することにより、陰極室に供給する原水のpHを低くして供給し、陰極室上部近傍および陰極吐出管のカルシウムの析出物を除去しようとするものである。
【0008】
また、陽極室から吐出する陰極水のpHを低くしてORP計の電極を保護することにより、正常運転に移行した場合、陽極室から吐水する陽極水のORPを直に正しく表示させようとするものである。
【0009】
【課題を解決するための手段】
本発明の電解水生成装置は、電解槽の原水供給側に電解質を供給する手段を設けると共に、イオン透過性隔膜で分割され、陰電極を挿入した陰極室と陽電極を挿入した陽極室との陰陽電極間に直流電圧を印加し、連続して電解槽に流入原水を電解し、陽極水吐出管に配設したORP計をもって陽極水使用の適合の是非を判断する電解水生成装置であって、上記手段と電解槽の間に原水供給管から分岐した流路を設け、該流路に薬剤供給手段を設けて、電解槽を逆洗するさい、少なくとも電解質を供給すると共に、該薬剤供給手段より有機酸を電解槽に供給した状態で逆洗を行うことを特徴とすることを要旨とするものである。
【0010】
【作用】
本発明の、逆洗中の原水に電解質を供給すると共に、電解槽に薬剤を添加した原水を供給することにより、正常運転中にできた陰極室上部近傍の電解電流密度の小さい領域や陰極吐出管のカルシウム析出物を溶解することができる。
【0011】
また、逆洗中に陽極室から吐水する陰極水のpHを低くして、陽極配管中に配設したORP計の電極を損傷しないようにする。
【0012】
しかも正常運転中は原水中の電解質の添加により、消毒および殺菌用洗浄用水を得ることができるものである。
【0013】
【実施例】
図1は図2に対照される本発明の一実施例である。図2と重複する動作説明は省く。
【0014】
図において、1は電解槽であり、8は水道水などの原水の流入を開閉するバルブであり、10は電解質供給槽9から原水に添加した電解質が混入した水が流れる給水管であり、11および12は上記電解質が混入された原水を電解槽の陰極室および陽極室に給水する給水管であり、13は陰極室の吐出管であり、14は陽極室の吐出管であり、15は吐出管14途中に配設された陽極吐水の性能を確認するORP計の電極であり、16は電解質供給槽9と電解槽との間に配設され、しかも給水管10から分岐した給水管17を介して薬剤を挿入する薬剤供給手段を構成する添加筒であり、18はその流出管であり、19は薬剤に供給する原水を開閉するバルブである。
【0015】
逆洗に際して、電解質を添加しながら逆洗する。そしてバルブ19を開放すると原水の一部は給水管17を介して添加筒16に流れ、添加筒に薬剤が収納されているときは薬剤を溶解して流出管18から給水管11、12を介して電解槽に供給される。
【0016】
電解槽は逆洗のため陰陽極には正常運転に対して正負が反対の電圧が印加されている。このため、陰極室には陽極水が、陽極室には陰極水が生成される。バルブ8が閉鎖された状態での逆洗では各々の生成水は陰極室または陽極室に滞留し、陰極室では室内の体積物の溶解がなされる。また、バルブ8が開放された状態での逆洗では各々の生成水は陰極室および陽極室から吐出し洗浄を行う。
【0017】
この際、陰極室に添加された薬剤は正常運転中にできた陰極室上部近傍の電解電流密度の小さい領域や陰極吐出配管のカルシウムの析出物を溶解することができる。
【0018】
逆洗中に陽極室から吐出する陰極水を中和してそのpHを低くし、陽極配管中に配設したORP計の電極の機能低下を防ぐことができる。
【0019】
なお、逆洗時のときのみ添加筒に薬剤を入れることにより、バルブ19を除去することができる。すなわち、逆洗に先立ち電解質の供給を停止すると共に添加筒に薬剤を供給する。その後バルブ8を開放して原水を供給することにより電解槽に薬剤が供給される。
【0020】
薬剤として有機酸が使用される。有機酸としてリンゴ酸やコハク酸なども使用できるが、好適にはクエン酸が使用できる。
【0021】
薬剤を挿入する添加筒は密閉性のある容器で、逆洗に先立ち、例えば、結晶状の上記クエン酸を詰める。これにより、逆洗の期間だけに上記有機酸を供給することができる。薬剤の供給量は添加筒の大きさにより任意に設定できる。
【0022】
【発明の効果】
本発明の構成により、逆洗中においても電解質を供給すると共に、原水に薬剤を添加して電解槽に供給することにより、正常運転中にできた陰極室上部近傍の電解電流密度の小さい領域や陰極吐出配管のカルシウムの析出物を溶解することができる。
【0023】
逆洗中に陽極室から吐出する陰極水を中和してそのpHを低くし、陽極配管中に配設したORP計の電極の機能低下を事前に防ぐことができる。
【0024】
この結果、装置を長期に亘りメインテナンスすることなく、所望により電解槽に流入する水に電解質を加えて電気分解を行い消毒および殺菌用洗浄用水を積極的に得ることができる。
【図面の簡単な説明】
【図1】本発明に関わる電解水生成装置の一実施例である。
【図2】電解水生成装置の従来例である。
【符号の説明】
1 電解槽
9 電解質供給槽
10 給水管
11 給水管
12 給水管
15 ORP計の電極
16 添加筒
18 流出口
19 バルブ
[0001]
[Industrial application fields]
The present invention relates to an apparatus that mainly uses anode water discharged from an anode chamber of an electrolyzed water generating apparatus that uses tap water as raw water. More specifically, the present invention relates to cleaning of deposits on the upper part of the cathode chamber and the cathode chamber discharge tube of such an apparatus and protection of the ORP electrode attached to the anode chamber discharge tube.
[0002]
[Prior art]
In the electrolyzed water generating apparatus shown in FIG. 2, the electrolyzer 1 is divided into a cathode chamber 3 and an anode chamber 4 by a diaphragm 2, and electrodes 5 and 6 are inserted into the husband's chamber to provide raw water such as tap water. Is supplied to the negative anode chamber through the water supply pipes 11 and 12 branched from the water supply pipe 10 after adding a predetermined amount of electrolyte from the electrolyte supply tank 9 to the water supply pipe 10. Raw water such as tap water supplied into the negative anode chamber is electrolyzed by energization of a direct current 7 applied between the electrodes, whereby the cathode water is electrolyzed in the cathode chamber and the anode water is electrolytically generated in the anode chamber. The electrolyzed negative anodized water is discharged from the discharge pipes 13 and 14 of the husband. The anode water discharge pipe 14 is provided with an ORP meter electrode 15 for confirming the ability of the discharged anode water.
[0003]
When a halogen compound such as NaCl or KCl is added to the raw water before supplying the electrolytic cell as an electrolyte at a certain ratio and electrolyzed in the electrolytic cell, the anion constituting the electrolyte moves to the anode chamber. As a result, the anode chamber HClO, ClO -, etc., anode water low pH containing plenty anions with disinfecting and sterilizing effect. Since this water has a disinfection and sterilization effect, it is used as cleaning water for disinfection and sterilization.
[0004]
However, in such an apparatus that mainly obtains anode water, cathode water having an extremely high pH is discharged along with the anode water. Although Ca ions exist in raw water such as tap water, Ca ions precipitate as calcium carbonate or calcium hydroxide in a high pH region, and gradually block the upper part of the electrolytic cell, the discharge pipe, and the like.
[0005]
For this reason, it stops the inflow of the electrolyte into the electrolytic cell every time the water is discharged for a certain period of time, and backwashing reverses the direction of the voltage applied to the negative anode, and deposits on the negative electrode and the cathode water in the cathode chamber. The calcium salt is washed and dissolved. As a result, the adhered calcium carbonate and calcium hydroxide are dissolved. However, even if the above cleaning is performed by this method, the region having a small electrolytic current density near the upper portion of the cathode chamber, the cathode discharge tube, and the like are not sufficiently back-washed, and there is a problem that the cleaning effect is difficult to achieve. In addition, if washing is performed only by backwashing, backwashing for a long time must be performed, and the electrolytic current during this time is wasted.
[0006]
During backwashing, the cathode water discharged from the anode chamber exhibits high pH alkalinity. The ORP meter installed in the anode chamber water discharge pipe is a device for measuring the oxidation-reduction potential of low pH acidic water. Since it is formed in an electrode structure suitable for this, it once touches high pH alkaline water. After that, an accurate value is no longer shown, or it takes a long time to show an accurate value. The anodized water user judges the capacity of the anodized water according to the display on the ORP meter. As described above, if the ORP meter display is not correct for a while even after the normal anodic water flows after the backwashing, the anodic water user drains the water discharged during that time. However, the anode water itself has an ORP indication that is not correct, and in fact, there is a possibility that water is discharged in a capacity state, and drainage during that time is wasted.
[0007]
[Problems to be solved by the invention]
Therefore, the present invention provides a chemical solution addition tank between the electrolyte supply tank and the electrolytic tank in an apparatus mainly using anodized water, and stores a chemical agent made of an organic acid in the chemical solution addition tank. At least, while adding an electrolyte to the raw water, supplying the above chemicals to the raw water, the pH of the raw water supplied to the cathode chamber is lowered, and calcium is deposited near the upper part of the cathode chamber and in the cathode discharge tube. It is intended to remove things.
[0008]
In addition, by protecting the ORP meter electrode by lowering the pH of the cathode water discharged from the anode chamber, when the operation is shifted to normal operation, the ORP discharged from the anode chamber is immediately displayed correctly. Is.
[0009]
[Means for Solving the Problems]
The electrolyzed water generating apparatus of the present invention is provided with means for supplying an electrolyte to the raw water supply side of the electrolytic cell, and is divided by an ion-permeable diaphragm, and includes a cathode chamber in which a negative electrode is inserted and an anode chamber in which a positive electrode is inserted. An electrolyzed water generating device that applies direct current voltage between the yin and yang electrodes, continuously electrolyzes the raw water flowing into the electrolytic cell, and determines whether or not the anodic water is suitable for use with an ORP meter disposed in the anodic water discharge pipe. A flow path branched from the raw water supply pipe is provided between the above means and the electrolytic tank, and a chemical supply means is provided in the flow path to supply at least an electrolyte and back the chemical tank, and the chemical supply means The gist is that backwashing is performed in a state in which an organic acid is supplied to the electrolytic cell.
[0010]
[Action]
According to the present invention, the electrolyte is supplied to the raw water during backwashing, and the raw water added with the chemical agent is supplied to the electrolytic cell, so that the area where the electrolysis current density is small in the vicinity of the upper part of the cathode chamber during normal operation and the cathode discharge. Calcium deposits in the tube can be dissolved.
[0011]
Further, the pH of the cathode water discharged from the anode chamber during backwashing is lowered so that the electrodes of the ORP meter disposed in the anode pipe are not damaged.
[0012]
Moreover, during normal operation, cleaning water for disinfection and sterilization can be obtained by adding an electrolyte in the raw water.
[0013]
【Example】
FIG. 1 is an embodiment of the present invention contrasted with FIG. The description of the operation overlapping that in FIG. 2 is omitted.
[0014]
In the figure, 1 is an electrolytic cell, 8 is a valve for opening and closing the inflow of raw water such as tap water, 10 is a water supply pipe through which water mixed with an electrolyte added to the raw water flows from an electrolyte supply tank 9, 11 And 12 are water supply pipes for supplying raw water mixed with the electrolyte to the cathode chamber and the anode chamber of the electrolytic cell, 13 is a discharge pipe for the cathode chamber, 14 is a discharge pipe for the anode chamber, and 15 is a discharge pipe. An ORP meter electrode for confirming the performance of the anode water discharge disposed in the middle of the pipe 14, 16 is disposed between the electrolyte supply tank 9 and the electrolytic tank, and further includes a water supply pipe 17 branched from the water supply pipe 10. An addition cylinder that constitutes a medicine supply means for inserting the medicine through, 18 is an outflow pipe, and 19 is a valve that opens and closes raw water supplied to the medicine.
[0015]
In backwashing, backwashing is performed while adding an electrolyte. When the valve 19 is opened, a part of the raw water flows into the addition cylinder 16 through the water supply pipe 17, and when the medicine is stored in the addition cylinder, the medicine is dissolved and discharged from the outflow pipe 18 through the water supply pipes 11 and 12. Supplied to the electrolytic cell.
[0016]
Since the electrolytic cell is backwashed, a negative and positive voltage is applied to the negative anode with respect to normal operation. For this reason, anode water is generated in the cathode chamber and cathode water is generated in the anode chamber. In backwashing with the valve 8 closed, each generated water stays in the cathode chamber or the anode chamber, and the volume in the chamber is dissolved in the cathode chamber. In backwashing with the valve 8 opened, each generated water is discharged from the cathode chamber and the anode chamber for cleaning.
[0017]
At this time, the chemical added to the cathode chamber can dissolve the deposits of calcium in the area near the upper portion of the cathode chamber having a low electrolytic current density and the cathode discharge pipe formed during normal operation.
[0018]
It is possible to neutralize the cathode water discharged from the anode chamber during backwashing to lower its pH, and to prevent the function of the ORP meter electrode disposed in the anode pipe from being lowered.
[0019]
In addition, the valve | bulb 19 can be removed by putting a chemical | medical agent in an addition cylinder only at the time of backwashing. That is, prior to backwashing, the supply of electrolyte is stopped and the chemical is supplied to the addition cylinder. Then, the chemical is supplied to the electrolytic cell by opening the valve 8 and supplying raw water.
[0020]
Organic acids are used as drugs. Malic acid and succinic acid can be used as the organic acid, but citric acid can be preferably used.
[0021]
The addition cylinder into which the drug is inserted is a hermetically sealed container, and is packed with, for example, the crystalline citric acid before backwashing. Thereby, the said organic acid can be supplied only in the period of backwashing. The supply amount of the medicine can be arbitrarily set according to the size of the addition cylinder.
[0022]
【The invention's effect】
With the configuration of the present invention, an electrolyte is supplied even during backwashing, and a chemical is added to the raw water and supplied to the electrolytic cell. Calcium deposits in the cathode discharge pipe can be dissolved.
[0023]
It is possible to neutralize the cathode water discharged from the anode chamber during the backwashing to lower its pH and prevent in advance the function of the ORP meter electrode disposed in the anode pipe.
[0024]
As a result, it is possible to positively obtain water for sterilization and sterilization by performing electrolysis by adding an electrolyte to the water flowing into the electrolytic cell as desired without performing maintenance for a long period of time.
[Brief description of the drawings]
FIG. 1 is an example of an electrolyzed water generating apparatus according to the present invention.
FIG. 2 is a conventional example of an electrolyzed water generating apparatus.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Electrolysis tank 9 Electrolyte supply tank 10 Water supply pipe 11 Water supply pipe 12 Water supply pipe 15 Electrode of ORP meter 16 Addition cylinder 18 Outlet 19 Valve

Claims (1)

電解槽の原水供給側に電解質を供給する手段を設けると共に、イオン透過性隔膜で分割され、陰電極を挿入した陰極室と陽電極を挿入した陽極室との陰陽電極間に直流電圧を印加し、連続して電解槽に流入した原水を電解し、陽極水吐出管に配設したORP計をもって陽極水使用の適合の是非を判断する電解水生成装置であって、上記手段と電解槽の間に原水供給管から分岐した流路を設け、該流路に薬剤供給手段を設けて、電解槽を逆洗するさい、少なくとも電解質を供給すると共に、該薬剤供給手段より有機酸を電解槽に供給した状態で逆洗を行うことを特徴とする電解水生成装置。A means for supplying the electrolyte is provided on the raw water supply side of the electrolytic cell, and a DC voltage is applied between the negative and positive electrodes divided by the ion-permeable diaphragm and between the cathode chamber in which the negative electrode is inserted and the anode chamber in which the positive electrode is inserted. An electrolyzed water generating apparatus for continuously electrolyzing raw water flowing into an electrolytic cell and judging whether or not to use anodic water using an ORP meter disposed in an anodic water discharge pipe, between the above means and the electrolytic cell A flow path branched from the raw water supply pipe is provided, a chemical supply means is provided in the flow path, and at the time of backwashing the electrolytic cell, at least an electrolyte is supplied and an organic acid is supplied from the chemical supply means to the electrolytic cell. The electrolyzed water generating apparatus characterized by performing backwashing in the state which carried out.
JP30698894A 1994-11-16 1994-11-16 Electrolyzed water generator Expired - Fee Related JP3641752B2 (en)

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JP3641752B2 true JP3641752B2 (en) 2005-04-27

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Cited By (1)

* Cited by examiner, † Cited by third party
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KR101206008B1 (en) 2010-12-10 2012-11-28 주식회사 지이플러스 Device and Method of disinfecting nutrient solution for plant factory

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101206008B1 (en) 2010-12-10 2012-11-28 주식회사 지이플러스 Device and Method of disinfecting nutrient solution for plant factory

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