JPH11267700A - Electrically sterilizing method - Google Patents

Electrically sterilizing method

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Publication number
JPH11267700A
JPH11267700A JP10119876A JP11987698A JPH11267700A JP H11267700 A JPH11267700 A JP H11267700A JP 10119876 A JP10119876 A JP 10119876A JP 11987698 A JP11987698 A JP 11987698A JP H11267700 A JPH11267700 A JP H11267700A
Authority
JP
Japan
Prior art keywords
sludge
human waste
water
turbidity
current
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.)
Pending
Application number
JP10119876A
Other languages
Japanese (ja)
Inventor
Hideo Tagawa
英生 田川
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.)
RYOYO SANGYO KK
Original Assignee
RYOYO SANGYO KK
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 RYOYO SANGYO KK filed Critical RYOYO SANGYO KK
Priority to JP10119876A priority Critical patent/JPH11267700A/en
Publication of JPH11267700A publication Critical patent/JPH11267700A/en
Pending legal-status Critical Current

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  • Apparatus For Disinfection Or Sterilisation (AREA)
  • Treatment Of Sludge (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PROBLEM TO BE SOLVED: To improve the capacity of human waste treatment and to reduce cost by sterilizing highly concentrated sludge flocculated to form floc by applying low voltage DC current to human waste septic tank sludge and simultaneously forming and recovering. SOLUTION: A small-sized lightweight human waste sludge concentrating device 11 is provided in a line for pulling out excess sludge. A titanium electrode as an anode and a stainless electrode as a cathode are provided in the human waste sludge concentrating device 11 and week DC current is applied between the electrodes. The human waste sludge is agglomerated to cause flocculation action by applying current to break the negatively charged hydration of the human waste sludge. A turbidity component is removed by the bond by van der Waals force with the flocculation action. The sludge has about pH 6.5-7 and then, the ζ-potential of the turbidity particle is neutralized to lower the turbidity and to increase a supernatant to be highly concentrated. The recovered sludge is easily reutilized because the sterilization effect occurs at the same time.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[産業上の利用分野]本発明はし尿浄化槽
汚泥を濃縮と同時に殺菌する方法及び放流水、清水、海
水中のウイルス、一般細菌を低電圧、直流電流により死
滅、殺菌する方法に関する。
[0001] The present invention relates to a method for concentrating and sterilizing sludge from human waste septic tanks and a method for killing and sterilizing viruses and general bacteria in effluent water, fresh water and seawater by low voltage and direct current.

【0002】[従来の技術]し尿浄化槽における余剰汚
泥抜取りは、従来定期的に回収しその処分、作業等に費
用が発生しているが、下水道網の整備に伴う負荷の過大
化と施設の増大化等経済的にも困難な状況下にあるが、
全く他の方法はみられていない現状である。放流水、清
水、海水中のウイルス、一般細菌についても同様であ
り、塩素殺菌に頼っているが、塩素の使用は極力減少さ
せる傾向にあるにも拘らず他に方法がない現状である。
2. Description of the Related Art Excessive sludge removal in a human waste septic tank has conventionally required periodic collection, disposal and operation, but costs have been incurred. Economic difficulties, etc.,
At present, no other method has been found. The same applies to viruses and general bacteria in effluent water, fresh water, and seawater. They rely on chlorine disinfection, but the use of chlorine tends to be reduced as much as possible, but there is no other method.

【0003】[発明の解決しようとする課題]本発明は
余剰汚泥の抜取り改善が下水処理場の処理容量と関連し
緊急課題とされているにも拘らず技術的に確立されてい
ない現状よりコストスペース等の施設全体の見直しを低
減し現状設備で運営することを課題とした。放流水には
塩素殺菌が行われているが河川、海洋生物への影響が大
きい。一方では清水中の有害徴生物、ウイルス、一般細
菌等の新種の出現によりO157騒動にみられるように
対策がなく塩素注入しても末端清水には死滅効果がなく
なっている現状である。海水中も同様であって外国から
の輸入魚、貝類に付着したウイルス等による在来種の魚
貝類が全滅していることを未然に防止する技術方法を提
供することを目的とする。
[0003] The present invention is more cost-effective than the present state, although the improvement of the removal of excess sludge is an urgent issue in relation to the treatment capacity of a sewage treatment plant, The task was to reduce the review of the entire facility, such as space, and to operate it with existing facilities. The effluent is chlorine-sterilized, but has significant effects on rivers and marine life. On the other hand, due to the emergence of new species such as pests, viruses, and general bacteria in fresh water, the terminal fresh water has no killing effect even if chlorine is injected without any countermeasures as seen in the O157 disturbance. The same applies to seawater, and it is an object of the present invention to provide a technical method for preventing native fish and shellfish from being completely annihilated by a virus or the like attached to a fish or shellfish imported from a foreign country.

【0004】[課題を解決するための手段]上述のよう
な目的を達成するために、本発明請求項1のし尿汚泥濃
縮装置は小型、軽量、取付容易、安全であり、チタン電
極、ステンレス電極を陽極及び陰極とし、直流を通電さ
せることでし尿汚泥の負電荷の水和をくずして、集塊さ
せ凝集作用を生じさせるものである。フアン・テア・ヴ
ァールスカによる結合の結果、濁度成分の除去が可能と
なった。汚泥のPHは6、5〜7程度であるので濁度粒
子のデータ電位が中和され濁度が低下し、上澄水が60
〜70%に増加して高濃縮が可能となった。同時に殺菌
効果が生じる結果、回収汚泥の再利用が容易となった。
請求項2の放流水、清水及び海水のウイルス、一般細菌
等の電気殺菌装置は小型、軽量、取付け容易、安全であ
り、チタン電極、ステンレス電極を陽極及び陰極とし直
流を通電させることで放流水、清水及び海水に塩素を発
生しない範囲で微少時間内に殺菌させることが可能とな
った。
[Means for Solving the Problems] In order to achieve the above object, the human waste sludge concentrating apparatus according to the first aspect of the present invention is small, lightweight, easy to install, and safe. Are used as an anode and a cathode, and when a direct current is applied, the hydration of the negative charge of the excreta sludge is broken to cause agglomeration and agglomeration action. The coupling by Juan Thea Varska made it possible to remove the turbidity components. Since the sludge has a pH of about 6, 5 to 7, the data potential of the turbidity particles is neutralized and the turbidity is reduced.
It was increased to 70%, enabling high concentration. At the same time, the sterilization effect was generated, and the reuse of the recovered sludge was facilitated.
The apparatus for sterilizing discharged water, freshwater and seawater viruses, general bacteria, and the like according to claim 2 is small, lightweight, easy to install, and safe, and discharges water by applying a direct current to a titanium electrode or a stainless steel electrode as an anode and a cathode. It is possible to sterilize within a very short time within a range that does not generate chlorine in fresh water and seawater.

【0005】[作用]本発明請求項1記載のし尿汚泥濃
縮装置は以下に述べるような作用がある。チタン電極、
ステンレス電極に微弱直流電流を通電することで、その
電気作用により化学物質の溶出のない無公害の高濃縮し
尿汚泥生成と同時殺菌が可能となった。本発明は汚泥の
負電荷の水和をくずして、集塊させる凝集作用の効果で
同時にフアン・デア・ヴァールスカによる結合により濁
度が低下し、上澄水が60〜70%に増加し高濃縮が可
能となった。撹拌作用が加わると更に沈降を早める結果
となった。希釈水も全く必要とせず現用し尿施設の能力
向上が期待される特長を有する。し尿は、PHは6、5
〜7程度のため最も凝集効果が良くアルミニュウム、ミ
ヨウバン、鉄類の添加も主く必要とせず加温設備も全く
不要であり、コスト的にも低減され費用の節減と汚泥抜
取りコストも低減された。電極の汚損防止のため約10
分毎に極性切替を行い、常に電極の清浄を行っている。
[Operation] The night soil sludge concentrating apparatus according to the first aspect of the present invention has the following operation. Titanium electrode,
By applying a weak DC current to the stainless steel electrode, the electric action made it possible to generate non-polluting, highly concentrated, urine sludge and simultaneous sterilization without elution of chemical substances. The present invention breaks down the hydration of sludge's negative charge and, at the same time, reduces the turbidity due to the binding effect by Juan der Varska due to the coagulation effect of agglomeration, increasing the supernatant water to 60-70% and increasing the high concentration. It has become possible. Addition of the stirring action resulted in further accelerated settling. It does not require any diluting water, and has the advantage of improving the capacity of existing human urine facilities. Night soil pH is 6,5
Approximately 7 so that the coagulation effect is the best and the addition of aluminum, alum and irons is not mainly required, and no heating equipment is required. The cost is reduced, the cost is reduced, and the sludge removal cost is reduced. . About 10 to prevent electrode contamination
The polarity is switched every minute, and the electrode is always cleaned.

【0006】本発明請求項2記載の放流水、清水、海水
の電気殺菌装置は以下に述べるような作用がある。放流
水の魚貝類等河川、海洋生物への影響が大きく、塩素注
入を極力制限してこれらを死滅させないように下水処理
場は心がけている状況である。しかしながら大腸菌の死
滅には塩素注入しか方法がなく本発明による殺菌効果が
期待されている。清水においては塩素殺菌法が採用され
ているが、トリハロメタン等有害物質の生成と塩素注入
量が少いと長距離給水管の末端では全く殺菌効果がない
場合が多くO157等の生存が人体に悪影響を与えてい
る。このため塩素注入量を増やすという逆効果が生じ安
全面からも対応に苦慮している現状であり、紫外線殺菌
ではランプの寿命よりコスト的に上昇し効果も万全では
ない。このため本発明の放流水、清水の使用末端におい
てチタン電極、ステンレス電極を交互に極性切替えを行
いながら直流を通電する結果、薬品、食塩等の補助剤を
一切使用せずウイルス、一般細菌の死滅が可能となっ
た。同様に海水では電気分解による塩素の発生が全くな
い範囲の直流を通電することで細胞−電極間電子移動反
応が生じ、陽電極において殺菌された。このためアサリ
貝、アコヤ貝、カキ等のウイルス障害等海中生物に有害
する新種ウイルス、一般細菌の死滅方法として注目され
ている。
The electric sterilizer for discharged water, fresh water and seawater according to claim 2 of the present invention has the following operation. The effluent has a great effect on rivers and marine organisms such as fish and shellfish, and the sewage treatment plant is trying to limit chlorine injection as much as possible and not kill them. However, Escherichia coli can be killed only by chlorine injection, and the bactericidal effect of the present invention is expected. In fresh water, chlorine sterilization method is adopted. However, if the generation of harmful substances such as trihalomethane and the amount of chlorine injected are small, there is often no sterilization effect at the end of the long distance water supply pipe, and the survival of O157 etc. has a bad effect on the human body. Have given. For this reason, the adverse effect of increasing the chlorine injection amount has occurred, and it is currently difficult to deal with the problem from a safety point of view. In the case of ultraviolet sterilization, the cost is longer than the life of the lamp, and the effect is not perfect. For this reason, as a result of applying a direct current while alternately switching the polarity of the titanium electrode and the stainless steel electrode at the end of use of the effluent water and fresh water of the present invention, viruses and general bacteria are killed without using any auxiliary agents such as chemicals and salt. Became possible. Similarly, in seawater, when a direct current in a range where no chlorine was generated by electrolysis was applied, an electron transfer reaction between the cell and the electrode occurred, and the cell was sterilized at the positive electrode. For this reason, it is attracting attention as a method for killing new viruses and general bacteria harmful to marine organisms such as virus damage to clams, pearl oysters, oysters, and the like.

【0007】[実施例]以下本発明の実施例を図面に基
づいて詳細に説明する。図1により第1実施例を説明す
る。この実施例では活性汚泥法の標準的工程を示す。し
尿1は調整槽2に集め均一化、PH調整後、ばつ気槽3
へ給液、散気用空気4を注入し、一定の滞留時間活性汚
泥により有機性物質に酸化分解される。活性汚泥はし尿
と混合されて沈殿槽5に入り2〜3時間滞留されて活性
汚泥を上澄液と分離し自然沈降される。沈殿槽5の上澄
液は放流水6として放流される。沈降汚泥は沈殿槽5の
下部中央に集め、ばつ気槽3へ返送汚泥7として返送汚
泥ポンプ8により循環使用される。ばつ気槽3内で汚泥
増殖量に相当する量は、余剰汚泥9として引抜かれ乾
燥、焼却、埋立て処分される。塩素注入器10は放流水
6を殺菌する。活性汚泥は微生物の集団でフロックを形
成しているので、有機物が吸着し微生物(細菌、カビ、
藻類)は自己の繁殖に必要なエネルギーを得て炭酸ガス
と水に酸化分解している。この吸着と酸化のバランスが
崩れると清澄な放流水が得られず濁る。フロックは活性
汚泥の外周に物理的に吸着されたもので0、7〜1×
1、5ミクロン程度でマイナスに帯電している。これに
直流を通電すると集塊しうる。余剰汚泥生成量は従来、
処理BOD(生物化学的酸素要求量)1k9当たり0、
3〜0、4kgであったが、本発明の採用により0、2
kg以下に約60%減少した。従来経費の60%が節減
される結果処理負荷も容量的に60%の余裕を生じたた
め施設の維持管理の安心感を生じ、下水道昔及に既存施
設で対応が可能となった効果が極めて大きい。極性切替
は可変式として10分間に極性切替を行った。
An embodiment of the present invention will be described below in detail with reference to the drawings. A first embodiment will be described with reference to FIG. This example shows a standard process of the activated sludge process. Human waste 1 is collected in the adjusting tank 2, and after homogenization, pH adjustment,
Then, the air 4 for aeration and aeration is injected into the reactor, and the activated sludge is oxidatively decomposed into organic substances by a fixed residence time. The activated sludge is mixed with human waste and enters the sedimentation tank 5, where it is retained for 2 to 3 hours to separate the activated sludge from the supernatant and settle naturally. The supernatant of the precipitation tank 5 is discharged as discharge water 6. The settled sludge is collected in the lower center of the sedimentation tank 5, and is returned to the hot air tank 3 and is circulated and used as return sludge 7 by the return sludge pump 8. The amount corresponding to the sludge multiplication amount in the steam tank 3 is withdrawn as excess sludge 9, dried, incinerated, and landfilled. The chlorinator 10 sterilizes the effluent 6. Activated sludge forms flocs in a group of microorganisms, so that organic matter is adsorbed and the microorganisms (bacteria, mold,
Algae) oxidize and decompose into carbon dioxide and water with the energy required for their own reproduction. If the balance between the adsorption and the oxidation is lost, clear effluent is not obtained and the water becomes turbid. Floc is physically adsorbed on the outer periphery of activated sludge and is 0, 7 to 1 ×
It is negatively charged at about 1.5 microns. When a direct current is applied to this, agglomeration may occur. The surplus sludge generation amount is conventionally
0 per 1 k9 of treated BOD (biochemical oxygen demand)
3-0, 4 kg, but 0, 2
It decreased by about 60% to less than kg. As a result of saving 60% of the conventional cost, the processing load has a margin of 60% in terms of capacity, resulting in a sense of security in the maintenance and management of the facility. . The polarity was switched for 10 minutes as a variable type.

【0008】次に図2により第2実施例についてに説明
する。この実施例では放流水、清水及び海水の電気殺菌
装置を示す。ポンプにより加圧された原水1は容器2の
中央に入り内周の陽極3を構成するチタン金網又はステ
ンレス金網網目を通過する。間隔片4は外周のチタン金
網又はステンレス金網で構成する陰極5へ通過する間に
ウイルス、一般細菌7を含んだ処理水7は死滅する効果
が生じる。この場合常温、常圧下の微弱電流加電であり
PH等の変化も生じない。チタン電極は白金メッキ、酸
化パラジュウムコーテイング等の処理により半永久的に
使用が可能となり極性切替装置8により約10分毎に陽
極、陰極を自動的に切替使用する。
Next, a second embodiment will be described with reference to FIG. In this embodiment, an electric sterilizer for discharged water, fresh water and seawater is shown. The raw water 1 pressurized by the pump enters the center of the container 2 and passes through a titanium wire mesh or a stainless steel wire mesh constituting the anode 3 on the inner periphery. While the spacing piece 4 passes through the outer periphery of the cathode 5 composed of a titanium wire mesh or a stainless wire mesh, the treated water 7 containing viruses and general bacteria 7 has an effect of killing. In this case, the weak current is applied at normal temperature and normal pressure, and there is no change in PH or the like. The titanium electrode can be used semi-permanently by processing such as platinum plating and palladium oxide coating, and the polarity switching device 8 automatically switches and uses the anode and the cathode approximately every 10 minutes.

【0009】以上の実施例によるし尿汚泥濃縮装置によ
って、次のような効果を奏した。 (1)大腸菌数2、600個/mlの余剰汚泥を陽極、
陰極夫々の電極面積1m電極間距離2mmとした容器
内の滞流時間60分では、上澄水が 60〜70%に増
加した。これを更に撹拌すると滞流時間40分でも上澄
水が同様60〜70%となった。撹拌することで凝集推
進効果が生じた。殺菌率はこの余剰汚泥を800ml/
分のポンプにより送水すると100%殺菌可能となっ
た。この場合電極は陽極と陰極が接触しないように間隙
片の絶縁ネットを間にはさみ、余剰汚泥が通過し易いよ
うにネット状の電極とした。加電圧は3V250mAで
あった。
The night soil sludge concentrator according to the above embodiment has the following effects. (1) Escherichia coli count 2, surplus sludge of 600 / ml as anode,
The residence time of 60 minutes in the vessel in which a cathode respective electrode area 1 m 2 electrode distance 2 mm, supernatant water is increased to 60% to 70%. When this was further stirred, the supernatant water became 60 to 70% even when the residence time was 40 minutes. Agitation produced a coagulation promoting effect. The sterilization rate is 800 ml /
When water was supplied by a pump for 100 minutes, 100% sterilization became possible. In this case, the electrodes were sandwiched by insulating nets of the gap pieces so that the anode and the cathode did not come into contact with each other, and were formed into net-like electrodes so that excess sludge could easily pass through. The applied voltage was 3 V, 250 mA.

【0010】次に以上の実施例による電気殺菌装置によ
って、次のような効果を奏した。 (1)放流水中の2、500個/mlの大腸菌数を塩素
殺菌せず本発明品により800ml/分で通水し直流電
圧3V500mAの通電により生菌数ゼロとした。 (2)清水中の一般細菌500個/mlを塩素ゼロの状
態とした後、800ml/分で通水し同じく直流電圧3
V500mAによって生菌数ゼロとした。 (3)海水中の一般細菌、ウイルスをアサリ貝殺菌海水
として使用するため、1、5v5mAにて海水容器3l
に15秒間浸漬の結果生菌数ゼロとなし得た。
Next, the electric sterilizer according to the above embodiment has the following effects. (1) The number of Escherichia coli at 2,500 cells / ml in the discharge water was passed at 800 ml / min by the present invention without chlorine sterilization, and the number of viable bacteria was reduced to zero by applying a DC voltage of 3 V and 500 mA. (2) 500 bacteria / ml of general bacteria in fresh water were brought to a state of zero chlorine, and then water was passed at 800 ml / min.
The number of viable bacteria was reduced to zero by V500 mA. (3) To use general bacteria and viruses in seawater as clam shellfish sterilized seawater, 3 liters of seawater container at 1.5v5mA
As a result of immersion for 15 seconds, the number of viable bacteria was zero.

【0011】本発明の実施例を図面に基づいて詳述して
きたが、本発明の具体的方法及びこの方法に用いられる
部材や装具類の具体的設計変更があっても本発明に含ま
れる。例えばチタン電極の直径、おりこみ方法、おりこ
み数量、表面処理、電極間距離電圧、電流、極性変換の
時間等任意に設定できる。又陽極、陰極の材質は任意で
あり塩素の発生を生じない範囲に使用される材質も付加
することが出来ると共に棒状として電極を構成すること
も含まれる。
Although the embodiment of the present invention has been described in detail with reference to the drawings, the present invention includes a specific method of the present invention and a specific design change of members and equipment used in the method. For example, it is possible to arbitrarily set the diameter of the titanium electrode, the method of insertion, the amount of insertion, the surface treatment, the voltage between the electrodes, the current, the time for polarity conversion, and the like. Further, the materials of the anode and the cathode are arbitrary, and materials used in a range in which generation of chlorine does not occur can be added, and the configuration of the electrode as a rod is included.

【0012】[発明の効果]本発明請求項1記載のし尿
汚泥濃縮装置では、前記方法を採用したため、従来下水
処理場において余剰汚泥の抜取り、産業廃棄物として焼
却すると地球温暖化原因となり、埋立すると廃水による
土壌汚染等が発生し、農業用コンポストとしての利用に
は乾燥工程が必要であり再利用できなかった。加えて下
水道の普及が推進される現代では、塩素による薬害の防
止に日夜研究がなされても対策はない状態である。余剰
汚染の抜取り減少は運搬車の減少、交通量の減少、排気
ガス汚染の減少と直結し、ランニングコストを低減し、
ばっ気槽、沈殿槽が現状のままで、下水道整備に伴う負
荷上昇にも充分対応しうる経済的な公共事業費負担が減
少する効果は日本国主体の利益として還元されることと
なり期待が極めて大きい。PHの変動、温度変化も発生
せす、電力的には極めて低く自然界電位としての生物体
の負電荷を利用するための方法であり、本発明適用以外
の他の場所への悪影響は全くみられないので安心であ
る。省エネルギー、省コスト省スペースに加え、チタン
は長期間使用出来ると共に回収しうるので回収チタンを
再利用することが可能となった。このような経済的効果
も極めて大きい。
[Effect of the Invention] In the night soil sludge concentrating apparatus according to the first aspect of the present invention, since the above-mentioned method is employed, if excess sludge is conventionally extracted at a sewage treatment plant and incinerated as industrial waste, it causes global warming and landfill. As a result, soil contamination and the like due to wastewater occurred, and a drying process was required for use as compost for agriculture, and it could not be reused. In addition, in modern times when the sewerage system has been promoted, there is no countermeasure even if research is conducted day and night to prevent the chemical damage caused by chlorine. The reduction of excess pollution is directly linked to the reduction of trucks, traffic volume and exhaust gas pollution, reducing running costs,
With the aeration tank and sedimentation tank remaining as they are, the effect of reducing the burden of economic public works expenses, which can sufficiently cope with the increase in load associated with sewerage development, will be returned to the interests of Japan itself, and expectations are extremely high. large. This is a method for utilizing the negative charge of an organism as a natural potential, which is extremely low in terms of electric power, which also causes pH fluctuation and temperature change, and has no adverse effect on other places other than the application of the present invention. There is no relief. In addition to energy and cost savings, titanium can be used for a long period of time and can be recovered, making it possible to reuse the recovered titanium. Such economic effects are also very large.

【0013】本発明請求項2記載の放流水、清水、海水
の電気殺菌方法では、前記方法を採用したため、本発明
を大型化することは極めて簡単であり大量処理が可能で
ある。放流水、清水、海水のいづれにも応用される結
果、水分野の環境に与える悪影響を未然に防止すること
が可能となった。
In the method for sterilizing discharged water, fresh water, and seawater according to the second aspect of the present invention, since the above method is employed, it is very easy to increase the size of the present invention, and large-scale treatment is possible. As a result of being applied to discharge water, freshwater, and seawater, it has become possible to prevent any adverse effects on the environment in the water field.

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

【図1】請求項1記載の方法に関する装置を示す説明図
である。
FIG. 1 is an explanatory diagram showing an apparatus relating to the method according to claim 1;

【図2】請求項2記載の方法に関する装置を示す説明図
である。
FIG. 2 is an explanatory view showing an apparatus relating to a method according to claim 2;

【符号の説明】[Explanation of symbols]

1、 し尿 図1 2、 調整槽 3、 ばっ気槽 4、 空気 5、 沈殿槽 6、 放流水 7、 返送汚泥 8、 返送汚泥ポンプ 9、 余剰汚泥 10、 塩素注入器 11、 し尿汚泥濃縮装置 1, human waste Fig. 12, adjustment tank 3, aeration tank 4, air 5, sedimentation tank 6, effluent 7, return sludge 8, return sludge pump 9, excess sludge 10, chlorinator 11, sewage sludge concentrator

【符号の説明】[Explanation of symbols]

1、 原水 図2 2、 容器 3、 陽極 4、 間隙片 5、 陰極 6、 処理水 7、 ウイルス、一般細菌 8、 極性切替装置 1, raw water Fig.2 2, container 3, anode 4, gap piece 5, cathode 6, treated water 7, virus, general bacteria 8, polarity switching device

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 し尿浄化槽汚泥を低電圧、直流電流によ
り凝集、フロック形成させた高濃度汚泥を殺菌して同時
に生成回収する方法を特徴とするし尿汚泥濃縮装置。
1. A human waste sludge concentrator characterized by a method of sterilizing a high-concentration sludge formed by coagulation and floc formation of a night soil sludge by a low voltage and a direct current and simultaneously producing and collecting the sludge.
【請求項2】 放流水、清水、海水中のウイルス、一般
細菌を低電圧、直流電流により死滅、殺菌する方法を特
徴とする放流水、清水、海水の電気殺菌装置。
2. An electric sterilizer for discharged water, fresh water, and seawater, which is characterized by killing and sterilizing viruses and general bacteria in the discharged water, fresh water, and seawater with a low voltage and a direct current.
JP10119876A 1998-03-25 1998-03-25 Electrically sterilizing method Pending JPH11267700A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10119876A JPH11267700A (en) 1998-03-25 1998-03-25 Electrically sterilizing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10119876A JPH11267700A (en) 1998-03-25 1998-03-25 Electrically sterilizing method

Publications (1)

Publication Number Publication Date
JPH11267700A true JPH11267700A (en) 1999-10-05

Family

ID=14772443

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10119876A Pending JPH11267700A (en) 1998-03-25 1998-03-25 Electrically sterilizing method

Country Status (1)

Country Link
JP (1) JPH11267700A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017058099A1 (en) * 2015-09-29 2017-04-06 Envirotech And Consultancy Pte. Ltd. Apparatus and method for treating wastewater

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017058099A1 (en) * 2015-09-29 2017-04-06 Envirotech And Consultancy Pte. Ltd. Apparatus and method for treating wastewater

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