JP2003136061A - Electrical water treatment device - Google Patents

Electrical water treatment device

Info

Publication number
JP2003136061A
JP2003136061A JP2001338106A JP2001338106A JP2003136061A JP 2003136061 A JP2003136061 A JP 2003136061A JP 2001338106 A JP2001338106 A JP 2001338106A JP 2001338106 A JP2001338106 A JP 2001338106A JP 2003136061 A JP2003136061 A JP 2003136061A
Authority
JP
Japan
Prior art keywords
water
seed crystal
scale
cathode
electrolytic cell
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.)
Granted
Application number
JP2001338106A
Other languages
Japanese (ja)
Other versions
JP4013527B2 (en
Inventor
Nobuhiro Oda
信博 織田
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP2001338106A priority Critical patent/JP4013527B2/en
Publication of JP2003136061A publication Critical patent/JP2003136061A/en
Application granted granted Critical
Publication of JP4013527B2 publication Critical patent/JP4013527B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide an electrical water treatment device which can prevent the deposition of scale on the surface of an electrode and scale trouble such as deterioration of an electric current value even in the case treating water containing components easily deposited as scale, such as hardness components, thereby maintaining a stable treatment over a long period of time, and to provide a scale component removing device which can efficiently remove the components easily deposited as the scale, such as the hardness components, only by electrical treatment without using chemicals. SOLUTION: This electrical treatment device treats water electrically by applying a direct current between a cathode 3 and an anode 2 disposed in an electrolytic cell 1. The electrical treatment device has a means by which the seed crystals of substances expected to be deposited on the surfaces of the electrodes 2, 3 or the their analogues are retained at least in the vicinity of the cathode 3.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、水槽内に配置した
陰極、陽極間に直流電流を通電することにより、該水槽
内の水を電気的に処理する電気的処理装置に係り、特
に、このような電気的処理装置における電極面へのスケ
ールの付着の問題を解決する水の電気的処理装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electric treatment apparatus for electrically treating water in a water tank by passing a direct current between a cathode and an anode arranged in the water tank. The present invention relates to a water electric treatment device that solves the problem of scale adhesion to the electrode surface in such an electric treatment device.

【0002】[0002]

【従来の技術】水槽内に配置した陰極、陽極間に直流電
流を通電することにより、該水槽内の水を電気的に処理
する電気的処理装置としては、次のようなものがある。 水を電気分解して水素と酸素又はオゾンを発生させ
る電気分解装置 塩水を電気分解して遊離塩素又は過酸化水素を発生
させる殺菌水製造装置 水を電気分解してイオン水を製造するイオン水製造
装置 汚水を電気分解して汚濁物を酸化分解する酸化分解
装置
2. Description of the Related Art The following is an electric treatment apparatus for electrically treating water in a water tank by passing a direct current between a cathode and an anode arranged in the water tank. Electrolytic device that electrolyzes water to generate hydrogen and oxygen or ozone Sterilized water manufacturing device that electrolyzes salt water to generate free chlorine or hydrogen peroxide Ionized water manufacturing that electrolyzes water to produce ionic water Equipment Oxidative decomposition equipment that electrolyzes waste water to oxidize and decompose pollutants

【0003】これらの電気的処理装置では、電気分解を
継続すると、主として水に含まれる硬度成分(カルシウ
ムイオン、マグネシウムイオンなど)が水酸化物を形成
してスケールとして電極面に付着し、電流値の低下、電
気分解効率の低下等のスケール障害を引き起こす。
In these electrical treatment apparatuses, when electrolysis is continued, hardness components (calcium ions, magnesium ions, etc.) mainly contained in water form hydroxides and adhere to the electrode surface as scales, resulting in a current value. And scale problems such as deterioration of electrolysis efficiency and electrolysis efficiency.

【0004】塩水を電気分解して遊離塩素を発生させる
殺菌水製造装置では、このようなスケールを防止するた
めに、一定時間毎に陽極と陰極を入れ替える転極という
操作が行われている。しかし、転極を行うためには、双
方の電極素材を高価な貴金属を用いた不溶性電極とする
必要があり、また、印加電圧を反転させるための制御シ
ステムを組み込む必要があり、装置が高価となるという
欠点がある。
In a sterilizing water production apparatus which electrolyzes salt water to generate free chlorine, an operation of reversing the anode and the cathode is performed at regular intervals to prevent such scale. However, in order to perform the polarity reversal, it is necessary to make both electrode materials insoluble electrodes using expensive noble metal, and it is necessary to incorporate a control system for reversing the applied voltage, which makes the device expensive. There is a drawback that

【0005】従来、水中の硬度成分を除去する方法とし
ては、イオン交換樹脂を用いた軟化処理や、pH調整と
種晶添加とを組み合わせた方法などがあるが、イオン交
換樹脂は再生のための薬品を必要とし、またpH調整の
ためにも薬品を必要とするため、薬品の調製(溶解)、
貯蔵、搬入、在庫管理等の手間を要する。
Conventionally, as a method for removing hardness components in water, there are softening treatment using an ion exchange resin, a method combining pH adjustment and seed crystal addition, and the like. Preparation of chemicals (dissolution), because chemicals are needed and also for pH adjustment
It takes time to store, carry in, and manage inventory.

【0006】[0006]

【発明が解決しようとする課題】本発明は上記従来の問
題点を解決し、硬度成分等の電極面でスケール化し易い
成分を含む水を処理する場合であっても、スケールを生
成させることなく、安定して処理を継続することができ
る水の電気的処理装置を提供することを目的とする。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems of the prior art, and does not generate scale even when treating water containing a component such as a hardness component that easily scales on the electrode surface. An object of the present invention is to provide an electrical treatment apparatus for water capable of stably continuing treatment.

【0007】本発明はまた、薬品を使用することなく、
ボイラ給水等の水中の硬度成分を除去することができる
スケール成分除去装置を提供することを目的とする。
The present invention also provides, without the use of chemicals,
An object of the present invention is to provide a scale component removing device capable of removing hardness components in water such as boiler feed water.

【0008】[0008]

【課題を解決するための手段】本発明の水の電気的処理
装置は、水槽と、該水槽内に配置された陰極及び陽極と
を有し、両極間に直流電流を通電することにより、該水
槽内の水を電気的に処理する電気的処理装置において、
該電極面に析出が予想される物質又はその類似物質の種
晶を少なくとも該陰極の近傍に存在させる手段を設けた
ことを特徴とする。
An electrical treatment apparatus for water according to the present invention comprises a water tank, a cathode and an anode arranged in the water tank, and a direct current is applied between both electrodes to obtain In an electrical treatment device that electrically treats the water in the aquarium,
A means for causing a seed crystal of a substance which is expected to be deposited or a substance similar thereto to exist on the electrode surface at least in the vicinity of the cathode is characterized.

【0009】電極面に析出することが予想される物質又
はその類似物質を種晶として存在させることにより、ス
ケールは、電極面で析出せずに、この種晶の表面で析出
するようになるため、電極面でスケール化することによ
るスケール障害は防止される。通常、スケールは、直流
電流の通電でアルカリ性となった陰極側に移動した水中
のカルシウムイオン、マグネシウムイオン等の硬度成分
が水酸化物を形成することにより陰極面で析出するもの
であり、従って、種晶は、陰極の近傍に存在させること
により、良好なスケール防止効果を得ることができる。
The presence of a substance which is expected to be deposited on the electrode surface or a substance similar thereto as a seed crystal causes the scale to deposit on the surface of this seed crystal instead of on the electrode surface. , Scale failure due to scaling on the electrode surface is prevented. Usually, the scale is a calcium ion in water that has moved to the cathode side that has become alkaline by the application of a direct current, hardness components such as magnesium ions are deposited on the cathode surface by forming a hydroxide, therefore, By allowing the seed crystal to exist in the vicinity of the cathode, a good scale preventing effect can be obtained.

【0010】本発明の電気的処理装置は、各種の電気分
解装置として好適であるが、水中の硬度成分を種晶表面
にスケールとして析出させることにより、ボイラ給水等
の水から硬度成分を除去するスケール成分除去装置とし
ても有効である。即ち、陰極の周辺には、カルシウムイ
オン等が移動してきてその濃度が高くなり、炭酸カルシ
ウム等のスケールが析出し易い条件となっている。従っ
て、水中の硬度成分から陰極近傍の種晶上にこれらのス
ケールが析出することにより、硬度成分が除去される。
このような薬品不使用のスケール成分除去装置を、例え
ば軟化装置の前処理装置として用いることにより、軟化
装置のイオン交換樹脂の負荷を軽減して、再生頻度、薬
品使用量を低減することができる。
The electric treatment apparatus of the present invention is suitable as various electrolyzers, but the hardness component in water is removed as a scale on the seed crystal surface to remove the hardness component from water such as boiler feed water. It is also effective as a scale component removing device. That is, the conditions are such that calcium ions and the like move around the cathode and the concentration thereof increases, and scales such as calcium carbonate are easily deposited. Therefore, the hardness component is removed by depositing these scales on the seed crystal near the cathode from the hardness component in water.
By using such a chemical-free scale component removing device as, for example, a pretreatment device of a softening device, it is possible to reduce the load of the ion exchange resin of the softening device and reduce the regeneration frequency and the amount of chemicals used. .

【0011】[0011]

【発明の実施の形態】以下に本発明の実施の形態を詳細
に説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described in detail below.

【0012】本発明において、電極面に付着が予想され
る物質(スケール)は、通常、水酸化カルシウム、水酸
化マグネシウム等であり、これらの粒子を種晶として使
用することができる。また、カルシウムやマグネシウム
を含有する難溶性化合物であっても種晶として作用する
ことから、炭酸カルシウム、硫酸カルシウム、炭酸マグ
ネシウム、炭酸マグネシウムカルシウム等、或いは、こ
れらを含有する鉱石等も種晶として使用することもでき
る。これらの種晶物質は、1種を単独で用いても良く、
2種以上を併用しても良い。
In the present invention, the substance (scale) expected to adhere to the electrode surface is usually calcium hydroxide, magnesium hydroxide or the like, and these particles can be used as seed crystals. Further, since even a sparingly soluble compound containing calcium or magnesium acts as a seed crystal, calcium carbonate, calcium sulfate, magnesium carbonate, magnesium calcium carbonate, or the like, or an ore containing these is also used as a seed crystal. You can also do it. These seed crystal substances may be used alone,
You may use 2 or more types together.

【0013】種晶の粒径は、その存在形態によっても異
なるが、通常、粒径0.1〜3mm程度の粒状であるこ
とが好ましい。
The grain size of the seed crystal varies depending on its existing form, but it is usually preferable that the grain size is about 0.1 to 3 mm.

【0014】種晶は、少なくとも陰極の近傍に存在させ
ることができれば良く、その存在形態には特に制限はな
く任意であるが、例えば、次のような方法を採用するこ
とができる。 電解槽内に懸濁状に保持する。この場合、処理水の
排出時に種晶が電解槽内に流出しないように、電解槽の
処理水流出口にネット等の透水性で種晶を通過させない
種晶流出防止部材を設けるか、或いは流出した種晶を処
理水から分離して電解槽に循環させる手段を設けること
が好ましい。 種晶を任意の支持材に固定して電解槽内に保持す
る。
The seed crystal has only to be present at least in the vicinity of the cathode, and its existing form is not particularly limited and may be arbitrary. For example, the following method can be adopted. Hold in suspension in the electrolytic cell. In this case, in order to prevent the seed crystal from flowing out into the electrolytic cell when the treated water is discharged, a seed crystal outflow prevention member such as a net that does not allow the seed crystal to pass through is provided at the treated water outlet of the electrolytic cell, or it has flowed out. It is preferable to provide means for separating the seed crystal from the treated water and circulating it in the electrolytic cell. The seed crystal is fixed to an arbitrary support material and held in the electrolytic cell.

【0015】なお、前述の如く、種晶は、電解槽内の全
域に存在する必要はなく、陰極の近傍に存在すれば良
い。
As described above, the seed crystal does not have to exist in the entire area of the electrolytic cell, but may exist in the vicinity of the cathode.

【0016】従って、種晶を電解槽内に懸濁状態で保持
する場合、例えば、種晶を陰極近傍のみに存在させるた
めに、電解槽の陰極側を透水性で種晶を通過させないセ
パレータ、例えば素焼きプレート、紙、樹脂等の多孔質
板により仕切り、陰極室を形成し、この陰極室内に種晶
を存在させるようにしても良い。
Therefore, when the seed crystal is held in suspension in the electrolytic cell, for example, in order to allow the seed crystal to exist only in the vicinity of the cathode, a separator that is water-permeable on the cathode side of the electrolytic cell and does not pass the seed crystal, For example, the cathode chamber may be formed by partitioning with a porous plate such as a unglazed plate, paper, resin, etc., and seed crystals may be present in this cathode chamber.

【0017】また、種晶を支持材に固定して保持する方
法としては、種晶を紙、樹脂等のシート状の支持材に接
着又は漉き込みにより固定して保持する方法が挙げられ
るが、この場合、このシート状支持材を陰極近傍に配置
することにより、種晶を陰極近傍に存在させることがで
きる。
As a method of fixing and holding the seed crystal on the support material, there is a method of fixing and holding the seed crystal on a sheet-shaped support material such as paper or resin by adhesion or polishing. In this case, by arranging this sheet-shaped support material in the vicinity of the cathode, the seed crystal can be made to exist in the vicinity of the cathode.

【0018】電極槽内の種晶は、静止状態ではなく、流
動状態ないし移動状態で存在させるのが好ましい。即
ち、種晶が静止状態であると新たに析出するスケールを
介して種晶同士或いは種晶と電極とが結合してスケール
障害に到るおそれがあるが、種晶を流動ないし移動状態
とすることにより、このような問題を防止することがで
きる。
It is preferable that the seed crystal in the electrode tank is not in a stationary state but in a fluid state or a moving state. That is, when the seed crystal is in a stationary state, the seed crystals may be bonded to each other or the seed crystal and the electrode through a newly deposited scale, which may lead to scale failure, but the seed crystal is made to flow or move. As a result, such a problem can be prevented.

【0019】従って、種晶を流動させるために、電解槽
又は電解槽の陰極室内の種晶を撹拌機による撹拌又は散
気管による曝気で流動させたり、種晶を水流により流動
させるために、種晶を電解槽に導入される被処理水の水
流、好ましくは上向流により流動させたり、電解槽内又
は電解槽外に設けたスラリーポンプにより、槽内水を循
環させるようにしても良い。種晶を被処理水の水流によ
り流動させる場合、種晶を被処理水と共に流動させ、電
解槽に導入される被処理水に種晶を添加し、電解槽から
取り出した処理水から種晶を固液分離して被処理水の導
入側に戻すようにしても良く、また、被処理水の上向流
により、電解槽内に種晶の流動床を形成するようにして
も良い。
Therefore, in order to make the seed crystal flow, the seed crystal in the electrolytic cell or the cathode chamber of the electrolytic cell is made to flow by stirring by a stirrer or aeration by an air diffuser, or in order to make the seed crystal flow in a water stream. The crystals may be made to flow by a water flow of the water to be treated introduced into the electrolytic cell, preferably an upward flow, or the water in the tank may be circulated by a slurry pump provided inside or outside the electrolytic cell. When the seed crystal is made to flow by the water flow of the water to be treated, the seed crystal is made to flow together with the water to be treated, the seed crystal is added to the water to be treated introduced into the electrolytic cell, and the seed crystal is extracted from the treated water taken out from the electrolytic cell. Solid-liquid separation may be performed and returned to the introduction side of the water to be treated, or a fluidized bed of seed crystals may be formed in the electrolytic cell by upward flow of the water to be treated.

【0020】また、電極板を若干傾斜させて設置し、種
晶を電極板上方から供給して、電極板上を下方に向かっ
て傾斜面に沿って移動させるようにしても良い。この場
合、電極板の下方に沈殿した種晶は、スラリーポンプ等
で上方に移動、循環させる。
Alternatively, the electrode plate may be installed with a slight inclination, the seed crystal may be supplied from above the electrode plate, and the seed crystal may be moved downward along the inclined surface. In this case, the seed crystal precipitated below the electrode plate is moved upward and circulated by a slurry pump or the like.

【0021】また、支持材に固定した種晶を移動させる
方法としては、種晶を固定した支持材を、任意の方法で
往復動又は回動させる方法が挙げられる。例えば、支持
材の上端を電解槽の槽壁の上端等に設けた懸架部材に固
定し、この懸架部材により陰極の近傍で支持材を往復動
させる方法や、支持材をロールに取り付け、このロール
を回転させる方法などを採用することができる。
As a method of moving the seed crystal fixed on the support material, there is a method of reciprocating or rotating the support material fixed on the seed crystal by an arbitrary method. For example, a method of fixing the upper end of the support material to a suspension member provided on the upper end of the cell wall of the electrolytic cell, and reciprocating the support material in the vicinity of the cathode by this suspension member, or attaching the support material to a roll, It is possible to adopt a method of rotating the.

【0022】このような種晶を固定した支持材の移動、
又は前述の懸濁状態の種晶の流動は、常時連続的に行う
必要はなく、種晶同士或いは種晶と電極板との間にスケ
ール化によるブリッジが形成される前に再流動又は再移
動させることができるような間隔で間欠的に行っても良
い。
The movement of the support material having such seed crystals fixed thereon,
Alternatively, the flow of the seed crystals in the above-mentioned suspended state does not have to be continuously performed at all times, and reflow or re-transfer is performed before the formation of a bridge due to scaling between the seed crystals or between the seed crystals and the electrode plate. You may perform intermittently at the intervals which can be made.

【0023】ところで、このように種晶の存在下で電気
分解を継続すると、種晶表面にスケール成分が析出して
種晶が次第に粗大化する。種晶を懸濁状態で電解槽内に
保持する場合、粗大化した種晶は、槽底部に沈降するよ
うになるため、適宜、槽底部から抜き出して粗大粒子を
排出することが望ましい。従って、このために、電解槽
の底部に種晶の沈降部となるピットと、このピットに連
絡する開閉弁付き種晶排出管を設け、定期的に又は必要
に応じて、種晶の粗大粒子を抜き出すことが好ましい。
或いは、スラリーポンプで種晶を流動させる場合、スラ
リーポンプによる種晶循環配管に開閉弁付き種晶抜き出
し配管を分岐して設け、定期的に又は必要に応じて、種
晶の粗大粒子を含む循環水の一部を抜き出すようにして
も良い。
By the way, when the electrolysis is continued in the presence of the seed crystal as described above, scale components are deposited on the surface of the seed crystal, and the seed crystal is gradually coarsened. When the seed crystals are held in the electrolytic cell in a suspended state, the coarsened seed crystals will settle at the bottom of the vessel, so it is desirable to appropriately withdraw from the bottom of the vessel to discharge coarse particles. Therefore, for this purpose, a pit that serves as a seed crystal settling portion and a seed crystal discharge pipe with an on-off valve that communicates with this pit are provided at the bottom of the electrolytic cell, and coarse particles of the seed crystal are regularly or as needed. Is preferably extracted.
Alternatively, when the seed crystals are made to flow by a slurry pump, a seed crystal extraction pipe with an opening / closing valve is branched and provided in the seed crystal circulation pipe by the slurry pump, and periodically or when necessary, a circulation containing coarse particles of the seed crystals. You may make it extract a part of water.

【0024】以下に図面を参照して本発明の電気的処理
装置の構成をより具体的に説明する。
The configuration of the electrical processing apparatus of the present invention will be described more specifically below with reference to the drawings.

【0025】図1(a)〜(c)は本発明の電気的処理
装置の実施の形態を示す概略的な断面図である。なお、
図1(a)〜(c)において、1は電解槽、2は陽極、
3は陰極、4は直流電源を示し、5は種晶を示す。
1 (a) to 1 (c) are schematic sectional views showing an embodiment of the electrical processing apparatus of the present invention. In addition,
In FIGS. 1A to 1C, 1 is an electrolytic cell, 2 is an anode,
3 is a cathode, 4 is a direct current power source, and 5 is a seed crystal.

【0026】図1(a)の装置は、電解槽1内に対面配
置された陽極2と陰極3との間に種晶5を投入し、この
種晶5を電解槽1に導入した被処理水の上向流と散気球
6からの曝気により流動させるようにしたものである。
処理水の排出口には、種晶の流出を防止するためのネッ
ト等の種晶流出防止部材7が設けられている。
In the apparatus shown in FIG. 1A, a seed crystal 5 is introduced between an anode 2 and a cathode 3 facing each other in an electrolytic cell 1, and the seed crystal 5 is introduced into the electrolytic cell 1 to be treated. It is made to flow by the upward flow of water and aeration from the diffuser bulb 6.
A seed crystal outflow preventing member 7 such as a net for preventing the outflow of the seed crystals is provided at the outlet of the treated water.

【0027】図1(b)の装置は、種晶5を被処理水の
上向流と、ポンプ8による循環で流動させるものであ
る。即ち、電解槽1内で沈降する種晶5は、ポンプ8で
電解槽1の底部から引き抜かれ、電解槽1の上部に循環
されることにより、電極2,3間で流動状態に保持され
る。この装置にあっても、処理水の排出口に種晶の流出
を防止するための流出防止部材7が設けられている。
The apparatus shown in FIG. 1 (b) causes the seed crystal 5 to flow by the upward flow of the water to be treated and the circulation by the pump 8. That is, the seed crystal 5 that settles in the electrolytic cell 1 is extracted from the bottom of the electrolytic cell 1 by the pump 8 and circulated in the upper part of the electrolytic cell 1, so that the seed crystal 5 is kept in a fluid state between the electrodes 2 and 3. . Even in this apparatus, an outflow prevention member 7 for preventing outflow of seed crystals is provided at the outlet of the treated water.

【0028】図1(c)の装置は、種晶5を被処理水と
共に流動させるものであり、被処理水と共に電解槽1内
に導入された種晶は、電解槽1内を上昇し、処理水と共
に電解槽1の上部から取り出された後、固液分離装置9
で処理水と分離され、分離された種晶が被処理水の導入
側に循環されるように構成されている。
The apparatus of FIG. 1 (c) causes the seed crystal 5 to flow together with the water to be treated, and the seed crystal introduced into the electrolytic cell 1 together with the water to be treated rises in the electrolytic cell 1, After being taken out from the upper part of the electrolytic cell 1 together with the treated water, the solid-liquid separation device 9
The separated seed crystals are circulated on the introduction side of the water to be treated.

【0029】いずれの装置においても、被処理水は電解
槽1の下部から導入されて槽内を上昇する間に電極2,
3で電気分解される。電気分解処理水は槽上部から排出
される。この電気分解処理において、被処理水中の硬度
成分は、電極2,3に析出することなく、電極2,3間
の種晶5の表面に析出するため、スケール障害は防止さ
れる。
In any of the devices, the water to be treated is introduced from the lower part of the electrolytic cell 1 and the electrode 2,
Electrolyzed at 3. The electrolyzed water is discharged from the upper part of the tank. In this electrolysis treatment, the hardness component in the water to be treated is not deposited on the electrodes 2 and 3, but is deposited on the surface of the seed crystal 5 between the electrodes 2 and 3, so that scale failure is prevented.

【0030】本発明の電気的処理装置は、水を電気分解
して水素と酸素又はオゾンを発生させる電気分解装置、
塩水を電気分解して遊離塩素又は過酸化水素を発生させ
る殺菌水製造装置、水を電気分解してイオン水を製造す
るイオン水製造装置、汚水を電気分解して汚濁物を酸化
分解する酸化分解装置等の様々な電気的処理装置に有効
であるが、水中の硬度成分を種晶表面にスケールとして
析出させることにより、ボイラ給水等の水から硬度成分
を除去するスケール成分除去装置としても好適であり、
このような薬品不使用のスケール成分除去装置を、例え
ば軟化装置の前処理装置として用いることにより、軟化
装置のイオン交換樹脂の負荷を軽減して、再生頻度、薬
品使用量を低減することができる。
The electroprocessing apparatus of the present invention is an electrolyzing apparatus for electrolyzing water to generate hydrogen and oxygen or ozone,
Sterilizing water production equipment that electrolyzes salt water to generate free chlorine or hydrogen peroxide, ion water production equipment that electrolyzes water to produce ionized water, oxidative decomposition that electrolyzes sewage to oxidatively decompose pollutants Although it is effective for various electric treatment devices such as equipment, it is also suitable as a scale component removal device for removing hardness components from water such as boiler feed water by precipitating hardness components in water as a scale on the seed crystal surface. Yes,
By using such a chemical-free scale component removing device as, for example, a pretreatment device of a softening device, it is possible to reduce the load of the ion exchange resin of the softening device and reduce the regeneration frequency and the amount of chemicals used. .

【0031】[0031]

【実施例】以下に実施例及び比較例を挙げて本発明をよ
り具体的に説明する。
EXAMPLES The present invention will be described more specifically with reference to Examples and Comparative Examples below.

【0032】実施例1、比較例1 電気伝導度:約20mS/m、硬度成分濃度:約50m
g/L(Ca硬度:35mg/L)の水を電解槽で電気
分解して遊離塩素を生成させる電気分解装置において、
本発明によるスケール防止効果を確認する実験を行っ
た。
Example 1, Comparative Example 1 Electric conductivity: about 20 mS / m, hardness component concentration: about 50 m
In an electrolyzer that electrolyzes water of g / L (Ca hardness: 35 mg / L) in an electrolytic cell to generate free chlorine,
An experiment was conducted to confirm the scale prevention effect according to the present invention.

【0033】用いた電解槽の構成は図1(a)に示す通
りであり、電極(陽極,陰極)としては、TiにPtメ
ッキを施した、寸法50mm×150mm×1mm厚さ
のものを用いた。電極間距離は10mmとし、電極間に
設けた散気球6により50mL/mmで曝気した。電解
槽の容量は80mLであり、水の流量は600mL/h
rとした。
The structure of the electrolytic cell used is as shown in FIG. 1 (a), and the electrodes (anode, cathode) having a size of 50 mm × 150 mm × 1 mm, in which Pt is plated on Ti, are used. I was there. The distance between the electrodes was 10 mm, and the air was diffused at 50 mL / mm by the air diffuser 6 provided between the electrodes. The electrolytic cell has a capacity of 80 mL and the flow rate of water is 600 mL / h.
r.

【0034】実施例1においては、種晶5として炭酸カ
ルシウム粒(粒径0.5mm)を電解槽1に投入し、電
極2,3間において曝気により流動させた。また、種晶
5が電解槽1から流出しないように、処理水の流出口部
分をサランネットで塞いだ。
In Example 1, calcium carbonate particles (particle size: 0.5 mm) as seed crystals 5 were placed in the electrolytic cell 1 and allowed to flow by aeration between the electrodes 2 and 3. Further, the outlet of the treated water was closed with a saran net so that the seed crystal 5 did not flow out of the electrolytic cell 1.

【0035】比較例1では、種晶は用いなかった。In Comparative Example 1, no seed crystal was used.

【0036】実施例1及び比較例1共に、電圧15Vを
印加し、初期電流は0.16Aで、処理水の遊離塩素濃
度は2.2mg/Lであった。
In both Example 1 and Comparative Example 1, a voltage of 15 V was applied, the initial current was 0.16 A, and the concentration of free chlorine in the treated water was 2.2 mg / L.

【0037】電圧15V一定で処理を継続したときの電
流及び処理水中の遊離塩素濃度及びカルシウム硬度の経
時変化を調べ、結果を表1に示した。
The changes over time in the current, the concentration of free chlorine in the treated water and the calcium hardness when the treatment was continued at a constant voltage of 15 V were examined, and the results are shown in Table 1.

【0038】また、電極面へのスケールの付着状況を調
べるために、30日間処理を継続した後、電極を酸で洗
浄し、洗浄液中のカルシウム量を測定し、結果を表1に
示した。
Further, in order to investigate the adhesion of scale to the electrode surface, after the treatment was continued for 30 days, the electrode was washed with acid and the amount of calcium in the washing solution was measured. The results are shown in Table 1.

【0039】[0039]

【表1】 [Table 1]

【0040】表1より次のことが明らかである。The following is clear from Table 1.

【0041】電解槽に種晶を投入しなかった比較例1で
は、電極面に多量のスケールが付着していることが確認
され、この電極面でのスケール析出のために経時による
電流値の低下が認められ、遊離塩素の発生量も低下し
た。
In Comparative Example 1 in which the seed crystal was not charged into the electrolytic cell, it was confirmed that a large amount of scale adhered to the electrode surface, and the current value decreased with time due to scale deposition on the electrode surface. Was observed, and the amount of free chlorine generated was also reduced.

【0042】これに対して、電解槽に種晶を投入した実
施例1では、電極面でのスケールの析出が防止され、電
流値の低下、遊離塩素の発生量の低下の問題はなかっ
た。
On the other hand, in Example 1 in which the seed crystal was put in the electrolytic cell, the scale was prevented from being deposited on the electrode surface, and there was no problem in that the current value was lowered and the amount of free chlorine generated was lowered.

【0043】しかも、実施例1では、硬度成分も除去さ
れており、従って、本発明の電気的処理装置は、スケー
ル成分除去装置としても有効であることが確認された。
Moreover, in Example 1, the hardness component was also removed, so it was confirmed that the electrical treatment apparatus of the present invention is also effective as a scale component removal apparatus.

【0044】[0044]

【発明の効果】以上詳述した通り、本発明の水の電気的
処理装置によれば、硬度成分等のスケール化し易い成分
を含む水を処理する場合であっても、電極面でのスケー
ルの析出、及び析出したスケールによる電流値の低下等
のスケール障害を防止して、長期に亘り安定な処理を継
続することができる。
As described in detail above, according to the electrical treatment apparatus for water of the present invention, even when water containing a component that easily scales, such as hardness component, is treated, the scale on the electrode surface can be reduced. It is possible to prevent scale failure such as precipitation and a decrease in current value due to the deposited scale, and to continue stable processing for a long period of time.

【0045】本発明によればまた、水中の硬度成分等の
スケール化し易い成分を、薬品を用いることなく、電気
的な処理のみで効率的に除去するスケール成分除去装置
が提供される。
According to the present invention, there is also provided a scale component removing device which efficiently removes components such as hardness components in water which are likely to be scaled, without using chemicals, only by electrical treatment.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の電気的処理装置の実施の形態を示す概
略的な断面図である。
FIG. 1 is a schematic cross-sectional view showing an embodiment of an electrical processing apparatus of the present invention.

【符号の説明】[Explanation of symbols]

1 電解槽 2 陽極 3 陰極 4 直流電源 5 種晶 6 散気球 7 種晶流出防止部材 8 ポンプ 9 固液分離装置 1 electrolysis tank 2 anode 3 cathode 4 DC power supply 5 seed crystals 6 air diffuser 7 Seed crystal outflow prevention member 8 pumps 9 Solid-liquid separator

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 9/02 619 B01D 9/02 619A C02F 5/00 620 C02F 5/00 620B 5/02 5/02 B 5/06 5/06 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) B01D 9/02 619 B01D 9/02 619A C02F 5/00 620 C02F 5/00 620B 5/02 5/02 B 5/06 5/06

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 水槽と、該水槽内に配置された陰極及び
陽極とを有し、両極間に直流電流を通電することによ
り、該水槽内の水を電気的に処理する電気的処理装置に
おいて、 該電極面に析出が予想される物質又はその類似物質の種
晶を少なくとも該陰極の近傍に存在させる手段を設けた
ことを特徴とする水の電気的処理装置。
1. An electric treatment apparatus comprising a water tank, a cathode and an anode arranged in the water tank, and electrically treating the water in the water tank by passing a direct current between both electrodes. A device for electrically treating water, characterized in that a means for causing seed crystals of a substance which is expected to be deposited or a substance similar thereto to exist on the electrode surface is present at least in the vicinity of the cathode.
【請求項2】 請求項1において、電気分解装置である
ことを特徴とする水の電気的処理装置。
2. An electric water treatment apparatus according to claim 1, which is an electrolyzer.
【請求項3】 請求項1において、スケール成分除去装
置であることを特徴とする水の電気的処理装置。
3. The water electric treatment device according to claim 1, wherein the electric water treatment device is a scale component removing device.
JP2001338106A 2001-11-02 2001-11-02 Water treatment equipment Expired - Fee Related JP4013527B2 (en)

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JP4013527B2 JP4013527B2 (en) 2007-11-28

Family

ID=19152646

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Country Status (1)

Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2014054815A1 (en) * 2012-10-01 2016-08-25 日本製紙株式会社 Continuous electrolysis method using electrolyzer for producing polysulfide and electrolysis apparatus for carrying out the method
CN112939154A (en) * 2021-01-26 2021-06-11 哈尔滨工业大学 Microbubble-aerated rotary electro-Fenton cathode and application thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2014054815A1 (en) * 2012-10-01 2016-08-25 日本製紙株式会社 Continuous electrolysis method using electrolyzer for producing polysulfide and electrolysis apparatus for carrying out the method
CN112939154A (en) * 2021-01-26 2021-06-11 哈尔滨工业大学 Microbubble-aerated rotary electro-Fenton cathode and application thereof

Also Published As

Publication number Publication date
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